IP Library Granted Patent US 9,550,675
Granted Patent B2
US 9,550,675 · App. 13/502,265 · Granted Jan 24, 2017

Method for removing a particulate contaminant material from a particulate mixed lithium metal phosphate material

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Quick Facts
Patent No.
US 9,550,675
App. No.
13/502,265
Granted
Jan 24, 2017
Kind
B2
Abstract

A method for removing a particulate contaminant material from a particulate mixed lithium metal phosphate material is provided. The method includes feeding the particulate mixed lithium metal phosphate material into a fluidizing stage containing particulate mixed lithium metal phosphate material of mass m, feeding the fluidized particulate mixed lithium metal phosphate material through a sifting stage, discontinuing the feed of the particulate mixed lithium metal phosphate material into the fluidizing stage after 10 to 100 times of the mass m have been fed into the fluidizing stage, fluidizing and sifting the material present in the fluidizing stage after discontinuing the feed until the mass of the material present in the fluidizing stage becomes 10% to 100% of the mass m, and removing the remaining material from the fluidizing stage.

Claims (23)

1. A method for removing a particulate contaminant material from a particulate mixed lithium metal phosphate material, comprising the steps of:

a) providing a particulate mixed lithium metal phosphate material, including a particulate contaminant material and a fine particulate mixed lithium metal phosphate, having a mass,

b) feeding the particulate mixed lithium metal phosphate material into a fluidizing stage and fluidizing it in the fluidizing stage, wherein the fluidized material in the fluidized stage has an average mass,

c) feeding the fluidized particulate mixed lithium metal phosphate material to a sifting stage and passing it through the sifting stage,

d) discontinuing the feed of the particulate mixed lithium metal phosphate material into the fluidizing stage after 10 to 100 times of mass m have been fed into the fluidizing stage,

e) fluidizing and sifting the material present in the fluidizing stage after discontinuing the feed, until the mass of the material present in the fluidizing stage becomes 10% to 100% of the mass m, and

f) removing the remaining material from the fluidizing stage, wherein

the mass of the particulate mixed lithium metal phosphate material provided in step a) is equal to x·m, in which x>100 and

the sequence of steps b) to f) is repeated until the total mass x·m has been processed.

2. The method according to claim 1 , wherein the feed of the particulate mixed lithium metal phosphate material into the fluidizing stage is discontinued after 30 to 70 times of the mass m have been fed into the fluidizing stage.

3. The method according to claim 1 , wherein the material present in the fluidizing stage is fluidized and sifted after discontinuing the feed, until the mass of the material present in the fluidizing stage becomes 20% to 80% of the mass m.

4. The method according to claim 1 , wherein the mixed lithium metal phosphate is represented by the formula LiMPO 4 , wherein M is selected from at least one metal selected from the group consisting of Fe, Sc, Ti, V, Cr, Mn, Co, Ni, Cu, Zn, Be, Mg, Ca, Sr, Ba, Al, Zr, La, and rare earth metals.

5. The method according to claim 4 , wherein M is selected from the group consisting of Fe, Mn, Co and Ni and mixtures thereof.

6. The method according to claim 5 , wherein M is Fe.

7. The method according to claim 1 , wherein the fine particulate mixed lithium metal phosphate consists of particles having a D 90 value of at most 25 μm.

8. The method according to claim 7 , wherein the fine particulate mixed lithium metal phosphate particles have a D 90 value of less than 0.8 μm.

9. The method according to claim 1 , wherein the particulate contaminant material is a metallic and/or oxide material.

10. The method according to claim 1 , wherein the fluidizing stage is a fluidized bed chamber.

11. The method according to claim 1 , wherein the method additionally comprises a step b1) of milling the particulate mixed lithium metal phosphate material in a milling step between the steps a) and b) or between b) and c).

12. The method according to claim 11 , wherein the milling step is carried out with a jet mill.

13. The method according to claim 11 , wherein the milling step is carried out in a milling stage and the fluidizing stage, the sifting stage and the milling stage are separate stages.

14. The method according to claim 13 , wherein the fluidizing stage, the sifting stage and the milling stage are integrated in one device.

15. The method according to claim 1 , wherein the fluidizing stage includes an automatic eject valve for removing the content of the fluidizing stage in step f).

Assignments (7)
CORRECTIVE ASSIGNMENT TO CORRECT THE DOCKET NUMBER PREVIOUSLY RECORDED ON REEL 69664 FRAME 66. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT OF ASSIGNORS INTEREST. Recorded Dec 30, 2024
From: JOHNSON MATTHEY PUBLIC LIMITED COMPANY
To: EPSILON CARBON PRIVATE LTD.
Reel/Frame 069813/0513 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 23, 2024
From: JOHNSON MATTHEY PUBLIC LIMITED COMPANY
To: EPSILON CARBON PRIVATE LTD.
Reel/Frame 069664/0066 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 17, 2023
From: EV METALS UK LIMITED
To: JOHNSON MATTHEY PLC
Reel/Frame 065613/0569 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 2, 2022
From: JOHNSON MATTHEY PLC
To: EV METALS UK LIMITED
Reel/Frame 062040/0255 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 22, 2015
From: CLARIANT INTERNATIONAL LTD
To: JOHNSON MATTHEY PLC
Reel/Frame 036853/0116 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 20, 2015
From: SUD-CHEMIE IP GMBH & CO. KG
To: CLARIANT INTERNATIONAL LTD
Reel/Frame 036832/0750 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 17, 2012
From: VOGLER, CHRISTIAN; BAUER, PETER; MICHOT, CHRISTOPHE
To: SUED-CHEMIE AG
Reel/Frame 028967/0298 →