IP Library Granted Patent US 7,226,885
Granted Patent B2
US 7,226,885 · App. 10/481,775 · Granted Jun 5, 2007

Method for producing gas diffusion electrodes

Assignees: Uhde GmbH; Gaskatel GmbH
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 7,226,885
App. No.
10/481,775
Granted
Jun 5, 2007
Kind
B2
Abstract

With the help of a method for production of a gaseous diffusion electrode from a silver catalyst on PTFE-substrate, it is endeavored to achieve results which can be reproduced, by avoiding the disadvantages of the state-of-the-art technology, whereby this is achieved in that the porous system of the silver catalyst is filled with a wetted fluid; a dimension-stable solid body with a grain size above that of the silver catalyst is mixed below the silver catalyst; the thus compression-stable mass is shaped into a homogenous catalyst band in a calender; and in a second calender step, an electrically conductive conductor material is imprinted into the catalyst band.

Claims (30)

1. Method for producing a gaseous diffusion electrode from a silver catalyst on a PTFE-substrate, comprising the steps of:

filling a porous system of the silver catalyst with a wetting fluid;

mixing a dimension-stable solid body with a grain size above that of the silver catalyst with the silver catalyst to produce a compression-stable mass;

shaping the thus obtained compression-stable mass into a homogeneous catalyst band in a calender, and

in a second calender step, imprinting an electrically conducting material into the catalyst band.

2. Method as per claim 1 , comprising

using as wetting fluid 5% isopropanol and as solid substance 30% ammonium carbonate or ammonium-hydrogen-carbonate and

driving both these filling substances out after producing the electrodes by means of an annealing step at preferably 110° C.

3. Method as per claim 1 , comprising

using as wetting fluid a tenside—preferably 5% triton X 100—, which penetrates into the porous system of the catalyst as well as reduces surface friction, so that the silver catalyst can glide out of a solidification zone and a dimension-stable ammonium carbonate and a PTFE-binder takes up a roller pressure.

4. Method as per claim 1 , comprising

using in the first calender step, a homogeneous catalyst band of thickness between 0.2–0.5 mm.

5. Method as per claim 1 , comprising

adjusting a roller gap to 350 μm and setting a roller feed to approx. 2 meters per minute.

6. Method as per claim 1 , comprising

using as electrical conducting material, a silver-coated nickel wire net with a string thickness of 0.15 mm and mesh width of 0.45 mm with an approx. 10 μm thick silver precipitate.

7. Method for producing a gaseous diffusion electrode from a silver catalyst on a PTFE-substrate, comprising the steps of:

filling a porous system of the silver catalyst with a wetting fluid;

mixing a dimension-stable solid body with a grain size above that of the silver catalyst with the silver catalyst to produce a compression-stable mass;

shaping the thus obtained compression-stable mass into a homogenous catalyst band in a calender,

in a second calender step, imprinting an electrically conducting material into the catalyst band; and

obtaining said gaseous diffusion electrode having large pores in the gaseous diffusion electrode, which ensures rapid gas transportation and smaller pores in the catalyst, which allow a homogeneous optimum utilisation of the catalyst.

8. Method as per claim 7 , comprising

using as wetting fluid 5% isopropanol and as solid substance 30% ammonium carbonate or ammonium-hydrogen-carbonate and driving both these filling substances out after producing the electrodes by means of an annealing step at preferably 110° C.

9. Method as per claim 7 , comprising

using as wetting fluid a tenside—preferably 5% triton X 100—, which penetrates into the porous system of the catalyst as well as reduces surface friction, so that the silver catalyst can glide out of a solidification zone and a dimension-stable ammonium carbonate and a PTFE-binder takes up a roller pressure.

10. Method as per claim 7 , comprising

using in the first calender step, a homogeneous catalyst band of thickness between 0.2–0.5 mm.

11. Method as per claim 7 , comprising adjusting a roller gap to 350 μm and setting a roller feed to approx. 2 meters per minute.

12. Method as per claim 7 , comprising using as electrical conducting material, a silver-coated nickel wire net with a string thickness of 0.15 mm and mesh width of 0.45 mm with an approx. 10 μm thick silver precipitate.

Assignments (2)
CHANGE OF NAME Recorded Feb 27, 2013
From: UHDE GMBH
To: THYSSENKRUPP UHDE GMBH
Reel/Frame 029884/0325 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 10, 2004
From: JANOWITZ, KOSMAS; DRESEL, TORSTEN; WOLTERING, PETER; BECKMANN, ROLAND; STEINMETZ, THOMAS; KIEFER, RANDOLF; DULLE, KARL-HEINZ; FUNCK, FRANK; KOHNKE, HANS-JOACHIM
To: UHDE GMBH; GASKATEL GMBH
Reel/Frame 015306/0279 →
Priority Claims (1)
DE 101 30 441 · Jun 23, 2001 · national
Continuity (1)
Related Publication 20040152588A1 · Aug 5, 2004