Method for recovering ruthenium from spent ruthenium-based catalyst carried on aluminum oxide

Patent metadata

Field	Value
Publication number	US-9758844-B2
Application number	US-201414479268-A
Country	US
Kind code	B2
Filing date	Sep 5, 2014
Priority date	Mar 5, 2012
Publication date	Sep 12, 2017
Grant date	Sep 12, 2017

Abstract

A method for recovering ruthenium from a spent ruthenium-based catalyst carried on aluminum oxide includes: drying, calcining, and cooling a spent catalyst; grinding the spent catalyst into black powder; placing the black powder in a fluidized bed reactor, purging the reactor with hydrogen and heating the black powder to obtain ruthenium metal, then heating the black powder in a mixed atmosphere of oxygen and ozone to obtain RuO 4 gas; absorbing the RuO 4 gas with a sufficient amount of hydrochloric acid to obtain a H 3 RuCl 6 solution; adding an excess oxidant to the H 3 RuCl 6 solution to oxidize the H 3 RuCl 6 into H 2 RuCl 6 ; adding excess NH 4 Cl to the H 2 RuCl 6 and then filtering, and washing the filter cake to obtain solid (NH 4 ) 2 RuCl 6 ; and reducing the solid (NH 4 ) 2 RuCl 6 by hydrogen to obtain ruthenium metal.

First claim

The invention claimed is:

1. A method for recovering ruthenium from a spent ruthenium-based catalyst carried on aluminum oxide, the method comprising:
1) drying a spent ruthenium-based catalyst carried on aluminum oxide at 100-150° C. in a nitrogen atmosphere for 1-2 hours, calcining the spent ruthenium-based catalyst carried on aluminum oxide at 300-500° C. for 2-4 hours, cooling the spent ruthenium-based catalyst carried on aluminum oxide to room temperature, and grinding the spent ruthenium-based catalyst carried on aluminum oxide into a black powder;
2) transferring the black powder to a fluidized bed reactor, purging the fluidized bed reactor with nitrogen for 20-40 minutes and then purging the fluidized bed reactor with hydrogen, and heating the black powder in a hydrogen atmosphere at a temperature of 200-400° C. and a pressure of 1-2 MPa for 2-3 hours to obtain a powder comprising ruthenium;
3) purging the fluidized bed reactor with nitrogen for 20-40 minutes, and then heating the powder comprising ruthenium in a mixed atmosphere of oxygen and ozone at a temperature of 500-750° C. and a pressure of 1-2 MPa for 1-8 hours to obtain a RuO 4 gas;
4) absorbing the RuO 4 gas with 3-8 mol/L hydrochloric acid to obtain a H 3 RuCl 6 solution;
5) adding an excess oxidant to the H 3 RuCl 6 solution, stirring the H 3 RuCl 6 solution for 0.5-1.5 hours to completely oxidize H 3 RuCl 6 into H 2 RuCl 6 to obtain a H 2 RuCl 6 solution, adding excess NH 4 Cl to the H 2 RuCl 6 solution and stirring at 60-90° C. for 1-3 hours to obtain a mixture, filtering the mixture to obtain a filter cake, and washing the filter cake to obtain solid (NH 4 ) 2 RuCl 6 , wherein the oxidant is a soluble chlorate; and
6) reducing the solid (NH 4 ) 2 RuCl 6 at a temperature of 450-800° C. in a mixed atmosphere of hydrogen and nitrogen to obtain ruthenium, wherein a volume fraction of hydrogen in the mixed atmosphere of hydrogen and nitrogen is 1-15%.

2. The method of claim 1 , wherein in 3), a space velocity of the mixed atmosphere of oxygen and ozone is 1000-4000 h −1 .

3. The method of claim 1 , wherein in 3), a volume fraction of the ozone in the mixed atmosphere of oxygen and ozone is 1-20%.

4. The method of claim 1 , wherein in 4), a concentration of the hydrochloric acid is 6 mol/L.

5. The method of claim 1 , wherein in 5), 1.2-2.5 times the theoretical weight of the NH 4 Cl that is required to completely react with the H 2 RuCl 6 solution is added to the H 2 RuCl 6 solution.

6. The method of claim 1 , wherein in 5), the oxidant is selected from the group consisting of ammonium chlorate, potassium chlorate, sodium chlorate, and magnesium chlorate.

7. The method of claim 1 , wherein in 5), the filter cake is washed with an ethanol solution.

8. The method of claim 1 , wherein in 5), the H 2 RuCl 6 solution is stirred at 100-400 revolutions per minute for 1-3 hours.

9. The method of claim 8 , wherein in 5), the H 2 RuCl 6 solution is stirred at 200 revolutions per minute for 1.5-2.5 hours.

10. The method of claim 2 , wherein in 3), a volume fraction of the ozone in the mixed atmosphere of oxygen and ozone is 1-20%.

11. The method of claim 2 , wherein in 4), a concentration of the hydrochloric acid is 6 mol/L.

12. The method of claim 2 , wherein in 5), 1.2-2.5 times the theoretical weight of the NH 4 Cl that is required to completely react with the H 2 RuCl 6 solution is added to the H 2 RuCl 6 solution.

13. The method of claim 2 , wherein in 5), the oxidant is selected from the group consisting of ammonium chlorate, potassium chlorate, sodium chlorate, and magnesium chlorate.

14. The method of claim 2 , wherein in 5), the filter cake is washed with an ethanol solution.

15. The method of claim 2 , wherein in 5), the H 2 RuCl 6 solution is stirred at 100-400 revolutions per minute for 1-3 hours.

16. The method of claim 15 , wherein in 5), the H 2 RuCl 6 solution is stirred at 200 revolutions per minute for 1.5-2.5 hours.

Assignees

• Wuhan Kaidi Eng Tech Res Inst

Inventors

• Lai Bo
• Xu Li
• Han Yiming
• Liu Qianqian
• Song Dechen

Classifications

• Y02P10/214

  Cross-Sectional Technologies · mapped topic

• C22B11/06 Primary

  Chloridising · CPC title

• C22B11/048

  from spent catalysts · CPC title

• C22B11/026 Primary

  from spent catalysts · CPC title

• Y02P10/20

  Recycling · CPC title