IP Library Granted Patent US 10,099,940
Granted Patent B2
US 10,099,940 · App. 14/690,709 · Granted Oct 16, 2018

Method of producing electrolytic manganese dioxide with high compact density and electrolytic manganese dioxide produced therefrom

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Quick Facts
Patent No.
US 10,099,940
App. No.
14/690,709
Granted
Oct 16, 2018
Kind
B2
Abstract

A method for producing electrolytic manganese dioxide with high compact density where electrolytic manganese dioxide pieces are milled in a classifying mill to produce first milled manganese dioxide particles where 30% of the particles are larger than 200 mesh and up to 95% of the particles are smaller than 325 mesh. The first milled manganese dioxide particles are milled a second time to produce manganese dioxide particles having a second particle size distribution. Also, an electrolytic manganese dioxide particle composition, wherein when the particle size distribution of the composition is plotted as a function of base-10 logarithm of the particle size, a first peak is centered at a particle size from 40-100 μm and contributes a minimum of 20% of the area under the curve of the overall particle size distribution and a maximum of 45% of the area under the curve of the overall particle size distribution.

Claims (26)

1. A method for producing electrolytic manganese dioxide comprising:

milling electrolytic manganese dioxide pieces in a classifying mill to produce first milled manganese dioxide particles, such that the first milled manganese dioxide particles have a particle size distribution where less than 30% of the first milled manganese dioxide particles are larger than 200 mesh and up to 95% of the first milled manganese dioxide particles are smaller than 325 mesh; and

milling the first milled manganese dioxide particles to produce second milled manganese dioxide particles,

wherein the second milled manganese dioxide particles have a second particle size distribution and wherein an alkaline potential of neutralized particles of the second milled manganese dioxide is no more than 20 mV less than an alkaline potential of neutralized particles of the first milled manganese dioxide.

2. The method of claim 1 , wherein 50-95% of the first milled manganese dioxide particles are smaller than 325 mesh.

3. The method of claim 1 , wherein less than 15% of the first milled manganese dioxide particles are larger than 200 mesh and up to 70% of the first milled manganese dioxide particles are smaller than 325 mesh.

4. The method of claim 3 , wherein 85-95% of the first milled manganese dioxide particles are smaller than 200 mesh and 50-70% of the first milled manganese dioxide particles are smaller than 325 mesh.

5. The method of claim 1 , wherein when particle size distribution of the first milled manganese dioxide particles is plotted as a function of base-10 logarithm of the particle size, the particle size distribution comprises a peak centered at a particle size greater than 45 μm that contributes at least 45% to the area under the curve of the overall particle size distribution.

6. The method of claim 5 , wherein the first peak is centered at a particle size greater than 55 μm and contributes at least 45% to the area under the curve of the overall particle size distribution.

7. The method of claim 1 , wherein the second milling is conducted for more than 2 minutes.

8. The method of claim 1 , wherein the second milling is conducted for less than 720 minutes.

9. The method of claim 1 , wherein when the second particle size distribution is plotted as a function of base-10 logarithm of the particle size, the particle size distribution comprises a first peak centered at a particle size from 40-100 μm, which contributes from 20% to 45% of the area under the curve of the overall particle size distribution.

10. The method of claim 1 , wherein a compact density of the second milled manganese dioxide particles is at least 1% greater than a compact density of the first milled manganese dioxide particles.

11. The method of claim 1 , further comprising neutralizing and/or drying the first milled manganese dioxide particles before the second milling.

12. The method of claim 1 , further comprising neutralizing and/or drying the second milled manganese dioxide particles.

13. The method of claim 1 , further comprising neutralizing the first milled manganese dioxide particles before the second milling and performing the second milling on neutralized, wet first-milled manganese dioxide particles.

14. The method of claim 13 , further comprising drying the second milled manganese dioxide particles.

15. The method of claim 1 , wherein a compact density of the second milled manganese dioxide particles is greater than a compact density of the first milled manganese dioxide particles.

16. A method for producing electrolytic manganese dioxide comprising:

milling manganese dioxide pieces to produce first milled manganese dioxide particles;

classifying the first milled manganese dioxide particles to produce classified manganese dioxide particles, wherein the classified manganese dioxide particles have a first particle size distribution; and

milling the classified manganese dioxide particles to produce second milled manganese dioxide particles,

wherein the second milled manganese dioxide particles have a second particle size distribution and wherein an alkaline potential of neutralized particles of the second milled manganese dioxide is no more than 20 mV less than an alkaline potential of neutralized particles of the first milled manganese dioxide.

17. An electrolytic manganese dioxide particle composition having a particle size distribution, wherein when the particle size distribution is plotted as a function of base-10 logarithm of the particle size, the particle size distribution comprises a first peak centered at a particle size of 40-100 μm and contributing 20-45 volume % to the area under the curve of the overall particle size distribution, a second peak centered at a particle size of 15-25 μm, and a third peak centered at a particle size of 0.1-1.0 μm and having a contribution of 1-20 volume % to the area under the curve of the overall particle size distribution.

18. The electrolytic manganese dioxide particle composition of claim 17 , wherein the first peak contributes 30-40 volume % to the area under the curve of the overall particle size distribution.

19. The electrolytic manganese dioxide particle composition of claim 17 , wherein the third peak contributes 8-20 volume % to the area under the curve of the overall particle size distribution.

Assignments (15)
RELEASE OF SECURITY INTEREST Recorded May 3, 2022
From: GOLDMAN SACHS LENDING PARTNERS LLC, AS COLLATERAL AGENT
To: PRINCE SPECIALTY PRODUCTS LLC (F/K/A PRINCE ERACHEM INC. AND PRINCE ERACHEM LLC); PRINCE MINERALS LLC; PRINCE ENERGY LLC
Reel/Frame 059802/0803 →
RELEASE OF SECURITY INTEREST Recorded May 3, 2022
From: GOLDMAN SACHS LENDING PARTNERS LLC, AS COLLATERAL AGENT
To: PRINCE SPECIALTY PRODUCTS LLC (F/K/A PRINCE ERACHEM INC. AND PRINCE ERACHEM LLC); PRINCE MINERALS LLC; PRINCE ENERGY LLC
Reel/Frame 059802/0808 →
SECURITY INTEREST Recorded May 2, 2022
From: CHROMAFLO TECHNOLOGIES CORPORATION; FERRO CORPORATION; FERRO ELECTRONIC MATERIALS INC.; PRINCE ENERGY LLC; PRINCE MINERALS LLC; PRINCE SPECIALTY PRODUCTS LLC
To: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, AS ADMINISTRATIVE AGENT
Reel/Frame 059845/0082 →
CHANGE OF NAME Recorded Nov 11, 2019
From: PRINCE ERACHEM LLC
To: PRINCE SPECIALTY PRODUCTS LLC
Reel/Frame 050978/0418 →
SECURITY INTEREST Recorded Jan 22, 2019
From: PRINCE ERACHEM LLC
To: GOLDMAN SACHS LENDING PARTNERS LLC, AS COLLATERAL AGENT
Reel/Frame 048089/0256 →
SECURITY INTEREST Recorded Jan 22, 2019
From: PRINCE ERACHEM LLC
To: GOLDMAN SACHS LENDING PARTNERS LLC, AS COLLATERAL AGENT
Reel/Frame 048089/0300 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 18, 2019
From: PRINCE ERACHEM INC.
To: PRINCE ERACHEM LLC
Reel/Frame 048058/0402 →
SECURITY INTEREST Recorded Apr 2, 2018
From: PRINCE ERACHEM INC.; PRINCE MINERALS LLC; PRINCE ENERGY LLC (FORMERLY GRINDING AND SIZING COMPANY LLC)
To: GOLDMAN SACHS LENDING PARTNERS LLC, AS COLLATERAL AGENT
Reel/Frame 045413/0473 →
RELEASE OF SECURITY INTEREST Recorded Apr 2, 2018
From: ABC FUNDING, LLC, AS AGENT
To: PRINCE ERACHEM INC. (F/K/A/ ERACHEM COMILOG, INC.)
Reel/Frame 045413/0446 →
SECURITY INTEREST Recorded Apr 2, 2018
From: PRINCE ERACHEM INC.; PRINCE MINERALS LLC; PRINCE ENERGY LLC (FORMERLY GRINDING AND SIZING COMPANY LLC)
To: GOLDMAN SACHS LENDING PARTNERS LLC, AS COLLATERAL AGENT
Reel/Frame 045413/0516 →
RELEASE OF SECURITY INTEREST Recorded Mar 30, 2018
From: MANUFACTURERS AND TRADERS TRUST COMPANY, AS AGENT
To: PRINCE ERACHEM INC. (F/K/A/ ERACHEM COMILOG, INC.)
Reel/Frame 045397/0410 →
SECURITY INTEREST Recorded Jun 2, 2017
From: PRINCE ERACHEM INC. (F/K/A ERACHEM COMILOG, INC.)
To: ABC FUNDING, LLC
Reel/Frame 042579/0596 →
CHANGE OF NAME Recorded May 10, 2017
From: ERACHEM COMILOG, INC.
To: PRINCE ERACHEM INC.
Reel/Frame 042322/0557 →
SECURITY INTEREST Recorded Jan 3, 2017
From: ERACHEM COMILOG, INC.
To: MANUFACTURERS AND TRADERS TRUST COMPANY
Reel/Frame 040830/0943 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 12, 2015
From: XU, BEI; SCHILLING, OLIVER; KEEL, KEITH A.
To: ERACHEM COMILOG, INC.
Reel/Frame 035827/0008 →