IP Library Granted Patent US 8,728,419
Granted Patent B1
US 8,728,419 · App. 13/757,252 · Granted May 20, 2014

Process for recycling alkaline batteries

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,728,419
App. No.
13/757,252
Granted
May 20, 2014
Kind
B1
Abstract

The invention relates to the recovery of manganese dioxide, zinc hydroxide/oxide and steel from metal cased alkaline dry cell batteries which have been wet crushed. There is also a process for recovery of the steel and high purity manganese dioxide which can be directly utilized in the electrode for alkaline dry cell batteries.

Claims (15)

1. A process for recovering high purity manganese dioxide from a slurry wherein alkaline batteries have been wet crushed and the casing particles have been removed which comprises the steps of;

1) filtering said slurry to obtain a filter cake;

2) treating the filter cake from step 1) with a solution of sulfuric acid to obtain a first product;

3) filtering the first product from step 2) to obtain a cake of insoluble manganese oxides and a filtrate and adjusting the pH of the filtrate to pH 3-5;

4) oxidizing the filtrate from step 3) to obtain a second product;

5) filtering the second product from step 4) to obtain a filtrate and treating the filtrate with a solution of sodium persulfate to precipitate manganese dioxide; and then

6) recovering the manganese dioxide.

2. The process of claim 1 which comprises adjusting the pH of the filtrate from step 3) with sodium hydroxide.

3. The process of claim 1 which comprises using air oxidation in step 4) at a pH of about 4 and at an elevated temperature.

4. The process of claim 1 which comprises treating the filter cake in step 2) with a 15 to 25% by weight solution of sulfuric acid.

5. The process of claim 1 comprising treating the filtrate of step 5) with an alkali hydroxide.

6. The process of claim 1 which comprises adjusting the pH of the filtrate of step 3) to pH 4-5 with sodium hydroxide and then adding sodium persulfate to form MnO 2 .

7. The process of claim 1 which comprises dewatering the filter cake from step 1) prior to treatment with a sulfuric acid solution.

8. The process of claim 1 wherein step 2) includes heating the slurry after the treatment with said sulfuric acid solution at an elevated temperature.

9. The process of claim 8 wherein said elevated temperature is 80° C.

Assignments (4)
SECURITY INTEREST Recorded Jul 3, 2024
From: CIRBA SOLUTIONS, LLC; CIRBA SOLUTIONS US, INC.; HERITAGE BATTERY RECYCLING, LLC; CIRBA SOLUTIONS SERVICES US, LLC; CIRBA SOLUTIONS SOUTH CAROLINA, LLC
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 067908/0930 →
CHANGE OF NAME Recorded Apr 1, 2024
From: RETRIEV TECHNOLOGIES INCORPORATED
To: CIRBA SOLUTIONS US, INC.
Reel/Frame 066971/0532 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 15, 2014
From: TOXCO, INC.
To: RETRIEV TECHNOLOGIES INCORPORATED
Reel/Frame 031975/0876 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 2, 2013
From: SMITH, W. NOVIS; ARUTUNIAN, MICHAEL; SWOFFER, SCOTT
To: TOXCO, INC.
Reel/Frame 030337/0970 →