IPC분류정보
국가/구분 |
United States(US) Patent
등록
|
국제특허분류(IPC7판) |
|
출원번호 |
UP-0574199
(2005-08-31)
|
등록번호 |
US-7713502
(2010-06-03)
|
우선권정보 |
DE-10 2004 041 997(2004-08-31) |
국제출원번호 |
PCT/EP2005/009359
(2005-08-31)
|
§371/§102 date |
20070823
(20070823)
|
국제공개번호 |
WO06/024507
(2006-03-09)
|
발명자
/ 주소 |
- Koehler, Joachim
- Zuber, Ralf
- Binder, Matthias
- Baenisch, Volker
- Lopez, Marco
|
출원인 / 주소 |
|
대리인 / 주소 |
Smith Gambrell & Russell LLP
|
인용정보 |
피인용 횟수 :
8 인용 특허 :
4 |
초록
▼
The invention relates to a process for recycling fuel cell components containing fluorine-containing and precious metal-containing constituents: in this process, the fluorine-containing constituents are separated off from the precious metal-containing constituents by treatment with a medium present
The invention relates to a process for recycling fuel cell components containing fluorine-containing and precious metal-containing constituents: in this process, the fluorine-containing constituents are separated off from the precious metal-containing constituents by treatment with a medium present in the supercritical state. Preference is given to using water as supercritical medium. After the fluorine-containing constituents have been separated off, the precious metal-containing residues can be recovered in a recycling process without harmful fluorine or hydrogen fluoride emissions. The fluorine-containing constituents can likewise be recovered. The process is used in the recovery of precious metals and/or fluorine-containing constituents from membrane fuel cells, electrolysis cells, batteries, sensors and other electrochemical devices.
대표청구항
▼
The invention claimed is: 1. Process for recycling fuel cell components containing fluorine-containing and precious metal containing constituents, wherein the fluorine-containing constituents are separated off from the precious metal-containing constituents by treatment with a medium present in the
The invention claimed is: 1. Process for recycling fuel cell components containing fluorine-containing and precious metal containing constituents, wherein the fluorine-containing constituents are separated off from the precious metal-containing constituents by treatment with a medium present in the supercritical state, and wherein the treatment is carried out using supercritical water in a temperature range from 350 to 450° C. and a pressure range from 200 to 400 bar. 2. Process according to claim 1 which further comprises steps for the comminution of the fuel cell components. 3. Process according to claim 1 which further comprises steps for the concentration and/or separation of the precious metals. 4. Process according to claim 1 which further comprises steps for the recovery and/or purification of the fluorine-containing constituents. 5. Process according to claim 3, wherein the steps for the concentration and/or separation of the precious metals comprise at least one of pyrolysis processes, melting processes, metallurgical smelting processes and wet chemical processes and/or combinations thereof. 6. Process according to claim 1, wherein the fluorine-containing constituents contain, a member selected from the group consisting of perfluorosulphonic acid polymers, fluorine-containing ionomer membranes, fluorine-containing ionomers, perfluorinated polymers, partially fluorinated polymers, fluorinated copolymers, PTFE dispersions, composite membranes with support fabrics made of fluorinated polymers, fluorinated wetting agents and fluorinated surfactants. 7. Process according to claim 1, wherein the precious metal containing constituents contain precious metals from the platinum group of the Periodic Table. 8. Process according to claim 1, wherein the reaction time is from 1 hour to 10 hours. 9. Process according to claim 1, wherein the medium present in the supercritical state is used in amounts up to a 1 000-fold excess, based on the mass of the fluorine-containing constituents. 10. Process according to claim 1, wherein the fluorine-containing constituents are extracted with water present in the supercritical state. 11. Process according to claim 1, wherein the fluorine-containing constituents are dissolved in the water present in the supercritical state. 12. Process according to claim 1, wherein the fuel cell components used are membranes coated with catalyst on one or both sides, catalyst coated gas diffusion layers, membrane-electrode units, membrane-electrode units with integrated bipolar plates, PEM fuel cell stacks, separated-off catalyst layers, paste residues, catalyst inks, catalyst residues and intermediate products and/or rejects from the manufacture of MEUs, CCMs and GDLs. 13. The process according to claim 1 further comprising recovering precious metals from fuel cell components. 14. The process according to claim 1 further comprising recovering fluorine-containing compounds from fuel cell components. 15. Process according to claim 1 wherein the precious metal is a member selected from the group consisting of platinum, ruthenium, palladium, rhodium, silver, gold, osmium, iridium and/or mixtures and alloys thereof. 16. Process according to claim 9 wherein water is used in amounts up to a 100 fold excess.
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