Method of recycling lead-acid storage battery

• US 6,730,428 B1
• Filed: 12/27/2001
• Issued: 05/04/2004
• Est. Priority Date: 07/24/1998
• Status: Expired due to Fees

• Current Assignee: K.K. Isonic
• Original Assignee: Hideki Sugiyama, T & K Company Limited
• Inventors: Sugiyama, Hideki, Kondo, Toshihiko
• Primary Examiner(s): Ryan, Patrick
• Assistant Examiner(s): Parsons, Thomas H.
• Application Number:
  US09/936,992
• Time in Patent Office: 859 Days
• Field of Search: 429/49, 205/63
• US Class Current: 429/49
• CPC Class Codes: H01M 10/06 Lead-acid accumulators semi-lead accumulators H01M10/20
• CPC Class Codes: H01M 10/4242 Regeneration of electrolyte or reactants
• CPC Class Codes: H01M 10/44 Methods for charging or discharging circuits for charging H02J7/00
• CPC Class Codes: H01M 10/54 Reclaiming serviceable parts of waste accumulators
• CPC Class Codes: Y02E 60/10 Energy storage using batteries
• CPC Class Codes: Y02W 30/84 Recycling of batteries or fuel cells

Abstract

The lead sulfate (PbSO₄) deposited on the surface of the positive electrode 18 or negative electrode 20 is reduced owing to the flow of the pulsating direct current from the positive electrode 18 toward the negative electrode 20 in the sullation removing step 34, while at the same time the positive electrode 18 of the lead-acid storage battery 10 is activated through the electrochemical doping in which the carbon suspension obtained by the electrolytic oxidation of the carbon positive electrode is used as at least a part of the battery electrolyte of the lead-acid storage battery 10 in the electrode activating step 40. Therefore, it is possible to select, as recyclable batteries, a wider range of used lead-acid storage batteries, so that even an used lead-acid storage battery which has a battery electrolyte whose specific gravity is considerably lowered and which accordingly appears to suffer from the sulfation can be recovered to have substantially the same capacity as that of a new lead-acid storage battery. Thus, the invention permits a wider range of the used lead-acid storage batteries to be recycled.

Claims

1. A method of recycling a lead-acid storage battery, to recover a capacity of said battery which has been reduced due to deposition of a lead sulfate on a surface of an electrode of said battery, said method comprising:

a first step of causing a pulsating direct current to flow from a positive electrode toward a negative electrode of said battery, for thereby reducing the lead sulfate deposited on the surface of said electrode; and

a second step of activating said positive electrode through an electrochemical doping in which a direct current voltage is applied to said battery with a carbon suspension being used as a battery electrolyte of said battery, said carbon suspension being obtained by electrolytic oxidation of a carbon positive electrode in a water system.

2. A method according to claim 1, wherein said pulsating direct current is caused to flow in said first step, by applying, to said battery, a pulsating direct current voltage which is sufficiently higher than a terminal voltage of said battery.

3. A method according to claim 2, wherein said pulsating direct current has a rectangular waveform.

4. A method according to claim 2, wherein said pulsating direct current has a sinusoidal waveform.

5. A method according to claim 2, wherein said pulsating direct current has a partially arcuate waveform.

6. A method according to claim 1, wherein said pulsating direct current is caused to flow from said positive electrode toward said negative electrode in said first step, for a time ranging from 12 to 24 hours.

7. A method according to claim 1, wherein said pulsating direct current used in said first step has a frequency ranging from 2 to 12 kHz.

8. A method according to claim 1, wherein said water system used in said second step consists of one of a pure water system and an aqueous solution of a dilute sulfuric acid.

9. A method according to claim 1, wherein said carbon suspension used in said second step consists of a colloidal suspension in which surfaces of carbon colloidal particles are chemically modified with a hydraulic group selected from a group consisting of a carbonyl group, a carboxyl group and a hydroxyl group.

10. A method according to claim 1, wherein said direct current voltage is applied to said battery in said second step such that an electric current flows from said positive electrode toward said negative electrode of said battery, by using a constant current.

11. A method according to claim 1, wherein said second saw in which said carbon suspension obtained by said electrolytic oxidation of said carbon positive electrode in said water system is added to said battery electrolyte of said battery is implemented before implementation of said first step in which said pulsating direct current is caused to flow from said positive electrode toward said negative electrode of said battery.

12. A method according to claim 1, wherein said water system used in said second step consists of an aqueous solution including a small amount of additive electrolyte which does not deteriorate performance of said lead-acid storage battery when said additive electrolyte is added to a battery electrolyte.

13. A method according to claim 1, wherein said direct current voltage is applied to said battery in said second step such that an electric current flows from said positive electrode toward said negative electrode of said battery, by using a pulsating current which changes in magnitude in a predetermined cycle.

14. A method according to claim 1, wherein said second step in which said carbon suspension obtained by said electrolytic oxidation of said carbon positive electrode in said water system is added to said battery electrolyte of said battery is implemented during implementation of said first step in which said pulsating direct current is caused to flow from said positive electrode toward said negative electrode of said battery.

15. A method according to claim 1, wherein said second step in which said carbon suspension obtained by said electrolytic oxidation of said carbon positive electrode in said water system is added to said battery electrolyte of said battery is implemented after implementation of said first step in which said pulsating direct current is caused to flow from said positive electrode toward said negative electrode of said battery.