IP Library › Granted Patent US 8,323,376
Granted Patent B2
US 8,323,376 · App. 12/513,707 · Granted Dec 4, 2012

Lead recycling

Assignee: Cambridge Enterprise Limited
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Quick Facts
Patent No.
US 8,323,376
App. No.
12/513,707
Granted
Dec 4, 2012
Kind
B2
Abstract

The present invention describes a method of recycling lead from lead containing waste, the method comprising the steps of mixing the battery paste with aqueous citric acid solution so as to generate lead citrate; isolating lead citrate from the aqueous solution; and converting the lead citrate to lead and/or lead oxide.

Claims (25)

1. A method for the recovery of lead from lead waste comprising one or more of Pb, PbO, PbO 2 , and PbSO 4 , the method comprising the steps of:

(a) treating the lead waste with aqueous citric acid solution so as to generate lead citrate;

(b) isolating lead citrate from the aqueous solution; and

(c) converting the isolated lead citrate to Pb and/or PbO.

2. The method according to claim 1 , wherein the lead citrate is Pb(C 6 H 6 O 7 ) and hydrates thereof, as well as the product of PbSO 4 treated with aqueous citric acid solution and aqueous trisodium citrate.

3. The method according to claim 1 wherein the lead waste is lead battery paste.

4. The method according to claim 1 wherein the pH of the aqueous citric acid solution is in the range pH 1.4 to 6 .

5. The method according to claim 1 wherein the aqueous citric acid solution additionally comprises a metal citrate.

6. The method according to claim 5 wherein the metal citrate is sodium citrate.

7. The method according to claim 1 wherein the aqueous citric acid solution additionally comprises hydrogen peroxide.

8. The method according to claim 7 wherein the lead waste comprises PbO and the mole ratio of PbO to hydrogen peroxide is in the range 1:0.1 to 1:4 and/or the mole ratio of PbO to citric acid is in the range 1:1 to 1:7 .

9. The method according to claim 1 wherein the temperature of the aqueous citric acid solution is maintained in the range 0 to 45° C.

10. The method according to claim 1 wherein the solid to liquid ratio of the lead waste to aqueous solution is in the range 1:1 to 1:50 w/w.

11. The method according to claim 1 wherein the isolated lead citrate is converted to Pb and/or PbO by calcination.

12. The method according to claim 11 wherein the calcination temperature is in the range 250 to 1,100° C.

13. The method according to claim 11 wherein the partial pressure of oxygen in the calcination is in the range to 0.01 to 5 atm.

14. A method of recycling a lead battery, the method comprising the steps of:

(a) obtaining lead battery paste from a lead battery;

(b) treating the lead battery paste with aqueous citric acid solution so as to generate lead citrate;

(c) isolating lead citrate from the aqueous solution;

(d) converting the isolated lead citrate to Pb and/or PbO; and

(e) incorporating the Pb and/or PbO into a battery plate.

15. The method according to claim 14 , wherein the lead citrate is Pb(C 6 H 6 0 7 ) and hydrates thereof, as well as the product of PbSO 4 treated with aqueous citric acid solution and aqueous trisodium citrate.

16. The method according to claim 14 wherein the lead citrate is isolated together with PbSO 4 .

17. The method according to claim 16 wherein the Pb and/or PbO includes PbSO 4 .

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 6, 2009
From: KUMAR, R. VASANT; KOTZEVA, VEGA P.; SONMEZ, M. SEREF
To: THE CHANCELLOR, MASTERS AND SCHOLARS OF THE UNIVERSITY OF CAMBRIDGE
Reel/Frame 022648/0082 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 6, 2009
From: THE CHANCELLOR, MASTERS AND SCHOLARS OF THE UNIVERSITY OF CAMBRIDGE
To: CAMBRIDGE ENTERPRISE LIMITED
Reel/Frame 022648/0210 →
Priority Claims (1)
GB 0622249.1 · Nov 8, 2006 · national
Continuity (1)
Related Publication 20100040938A1 · Feb 18, 2010