Apparatus for manufacturing potassium compound and method of recovering potassium compound from brine

Patent metadata

Field	Value
Publication number	US-10046302-B2
Application number	US-201414909436-A
Country	US
Kind code	B2
Filing date	Jul 30, 2014
Priority date	Jul 31, 2013
Publication date	Aug 14, 2018
Grant date	Aug 14, 2018

Abstract

The present invention relates to an apparatus for manufacturing a potassium compound and a method of recovering a potassium compound from a brine, and provides the apparatus for manufacturing the potassium compound, including: a continuous pre-treatment apparatus including a crushing portion, a pulverization portion, and a particle size separation portion for processing a mixed raw material salt obtained after lithium, magnesium, and calcium are extracted from a brine to have a particle size for easy separation and sorting; a continuous potassium compound lump recovering apparatus continuously separating and recovering the potassium compound from the pre-treated mixed raw material salt; a continuous potassium compound separating and sorting apparatus continuously separating and sorting potassium chloride and a glaserite (Na2SO4.3K2SO4) from the recovered potassium compound; and a continuous potassium sulfate conversion apparatus extracting potassium sulfate from the separated glaserite.

First claim

The invention claimed is:

1. An apparatus for manufacturing a potassium compound, comprising:
a pre-treatment apparatus for processing a mixed raw material salt obtained from a brine to form a pre-treated mixed raw material salt including a potassium compound;
a potassium compound recovering apparatus for separating and recovering the potassium compound from the pre-treated mixed raw material salt;
a potassium compound separating and sorting apparatus for separating and sorting potassium chloride and a glaserite (Na 2 SO 4 .3K 2 SO 4 ) from the recovered potassium compound; and
a potassium sulfate conversion apparatus for extracting potassium sulfate from the separated glaserite,
wherein the potassium compound recovering apparatus includes a potassium compound floating and sorting apparatus,
wherein the potassium compound floating and sorting apparatus includes
a plurality of cells for sorting,
a diffuser equipped in each of the cells to suck external air while rotating to form small bubbles in a slurry solution;
a scraper for recovering the floated potassium compound, and
a floating assistor applying ultrasonic wave vibration at a lower end of the cell to improve separation efficiency and purity.

2. The apparatus of claim 1 , wherein
the potassium compound recovering apparatus includes:
a raw material addition apparatus for adding the mixed raw material salt, saturated brine, and a floatation reagent into the potassium compound floating and sorting apparatus;
a conditioner for mixing the mixed raw material salt and the saturated brine to manufacture a slurry and mixing the floatation reagent therewith;
the potassium compound floating and sorting apparatus for injecting bubbles into a slurry solution where the mixed raw material salt, the saturated brine, and the floatation reagent are mixed to float the potassium compound and thus perform sorting; and
a solid-liquid separation apparatus for performing solid-liquid separation of the sorted potassium compound and the residual slurry.

3. The apparatus of claim 2 , wherein,
the conditioner mixing the mixed raw material salt and the saturated brine to manufacture the slurry and mixing the floatation reagent therewith is configured such that the mixed raw material salt is added at a weight ratio of 0.1 to 0.2 based on the saturated brine.

4. The apparatus of claim 2 , wherein
the floatation reagent is sodium dodecyl sulfate.

5. The apparatus of claim 4 , wherein
the potassium compound floating and sorting apparatus is configured such that the floatation reagent is added at a weight ratio of 0.01 to 0.05 relative to the slurry solution.

6. The apparatus of claim 2 , further comprising
a conduit operable to recirculate a filtrate separated through the solid-liquid separation apparatus performing solid-liquid separation of the sorted potassium compound and residual slurry including the saturated brine to the raw material addition apparatus.

7. The apparatus of claim 1 , wherein
the plurality of cells are connected in series, and
the separated and sorted slurry solution is passed from one cell in the plurality of cells to the next cell to improve the purity of the potassium compound.

8. The apparatus of claim 1 , wherein
the diffuser includes an air inflow adjustment valve.

9. The apparatus of claim 1 , wherein
the diffuser is configured such that a rotation speed of the diffuser is 10 to 200 rpm.

10. The apparatus of claim 1 , wherein
the potassium compound separating and sorting apparatus includes:
a raw material addition apparatus for adding the potassium compound and a specific gravity liquid into a mixing machine;
the mixing machine for mixing the added potassium compound and specific gravity liquid to manufacture a slurry;
a potassium compound specific gravity sorting apparatus for separating potassium chloride and the glaserite by using a specific gravity difference of the potassium compound; and
a solid-liquid separation apparatus for performing solid-liquid separation of sorted potassium chloride and glaserite.

11. The apparatus of claim 10 , wherein the mixing machine mixing the added potassium compound and the specific gravity liquid to manufacture a slurry is configured such that a specific gravity of the specific gravity liquid is 2.3 to 2.4.

12. The apparatus of claim 10 , wherein
the mixing machine mixing the added potassium compound and specific gravity liquid to manufacture the slurry is configured such that a weight ratio of the potassium compound is 0.1 to 0.4 relative to specific gravity liquid.

13. The apparatus of claim 10 , wherein
the mixing machine further includes a proportional control valve for adjusting an amount of the slurry added into the potassium compound specific gravity sorting apparatus at a predetermined speed.

14. The apparatus of claim 10 , wherein
the potassium compound slurry flows into an intermediate portion of the potassium compound specific gravity sorting apparatus, and
the apparatus further includes:
a potassium chloride outlet of an upper portion of the specific gravity sorting apparatus, in which potassium chloride having a small specific gravity is floated and thus withdrawn; and
a glaserite outlet of a lower portion of the specific gravity sorting apparatus, in which the glaserite having a large specific gravity descends and thus is withdrawn.

15. The apparatus of claim 10 , further comprising
a conduit operable to recirculate a filtrate separated by performing solid-liquid separation of sorted potassium chloride and glaserite by the solid-liquid separation apparatus including the specific gravity liquid to the raw material addition apparatus adding the potassium compound and the specific gravity liquid into the mixing machine.

16. The apparatus of claim 1 , wherein
the potassium sulfate conversion apparatus extracting potassium sulfate from the separated glaserite includes:
a raw material addition apparatus for adding the separated glaserite and a saturated potassium chloride aqueous solution;
a potassium sulfate reactor for manufacturing potassium sulfate from the glaserite; and
a solid-liquid separation apparatus for performing solid-liquid separation of manufactured potassium sulfate.

17. The apparatus of claim 16 , wherein
the potassium sulfate reactor manufacturing potassium sulfate from the glaserite includes
a first reaction bath, a second reaction bath, and
a reaction mixer positioned at lower portions of the first and second reaction baths to allow a slurry to enter and then perform agitation and thus induce a reaction.

18. The apparatus of claim 17 , wherein
the first reaction bath and the second reaction bath include:
a partition positioned between the first reaction bath and the second reaction bath;
a flow path formed at a lower portion of the partition; and
an outlet positioned at an upper portion of the other side wall of the partition at which the flow path is formed,
wherein the first reaction bath is constituted so that the slurry enters at an upper portion and flows through the flow path at the lower portion of the partition existing between the first reaction bath and the second reaction bath from the first reaction bath to the second reaction bath, and the second reaction bath is constituted so that the outlet exists at the upper portion of the other side wall of the partition therein to allow the slurry flowing thereinto from the first reaction bath to flow to the outside.

19. The apparatus of claim 17 , wherein
the reaction mixer is const

Assignees

• Res Inst Ind Science & Tech
• Posco
• Mpply Co Ltd

Inventors

• Chon Uong
• Han Gi-Chun
• Lee Im Chang
• Kim Ki Young
• Park Woon Kyoung

Classifications

• B01J19/24 Primary

  Stationary reactors without moving elements inside (B01J19/08, B01J19/26 take precedence; with stationary particles B01J8/02) · CPC title

• C01D5/02 Primary

  Preparation of sulfates from alkali metal salts and sulfuric acid or bisulfates; Preparation of bisulfates · CPC title

• C01D3/06

  Preparation by working up brines; seawater or spent lyes · CPC title

• B03D1/1431

  Dissolved air flotation machines · CPC title

• C01D3/08

  Preparation by working up natural or industrial salt mixtures or siliceous minerals · CPC title