IP Library Patent Application 12528511
Patent Application
App. No. 12/528,511

REFORMING CATALYST FOR MOLTEN CARBONATE FUEL CELLS

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 None
App. No.
12/528,511
Abstract

The present invention relates to a catalyst composition and a catalyst material which are suitable for use as a reforming catalyst in a fuel cell and are less susceptible to catalyst poisoning by alkali metals. The invention also relates to a catalyst suspension for the preparation of the catalyst composition and the catalyst material, plus a process for the preparation of the catalyst suspension and the catalyst composition. The invention is also directed towards the use of the catalyst composition or the catalyst material in a fuel cell.

Claims (37)

1 . Catalyst composition for methane steam reforming, comprising an Ni catalyst and a binding agent, characterized in that the catalyst has a pore volume of at least 200 mm 3 /g.

2 . Catalyst composition according to claim 1 , wherein the pore volume lies between 700 and 800 mm 3 /g.

3 . Catalyst composition according to claim 1 , wherein the catalyst comprises particles having a particle size with a d 50 value of 2 to 10 μm.

4 . Catalyst composition according to claim 3 , wherein the d 50 value lies between 2 and 5 μm.

5 . Catalyst composition according to claim 1 , wherein the catalyst comprises nickel, silicon and aluminium.

6 . Process for the preparation of the catalyst composition for methane steam reforming claim 1 , comprising the steps of

preparing a suspension comprising a binding agent and an Ni catalyst powder in a dispersing medium,

adding a burnout material to the suspension, and

then heating the mixture to produce the catalyst composition.

7 . Process according to claim 6 , wherein an organic polymer, preferably cellulose, comprises the binding agent and a sol comprises the burnout material.

8 . Process according to claim 6 , wherein the process further comprises applying the suspension to a carrier prior to the heating step.

9 . Process according to claim 6 , wherein the heating comprises drying and/or calcining, preferably at 300-400° C.

10 . (canceled)

11 . (canceled)

12 . Process according to claim 6 , wherein the dispersing medium comprises water.

13 . Process according to claim 6 , wherein the suspension is wet-ground before or after the addition of the binding agent.

14 . Process according to claim 6 , wherein the burnout material is added before, after or at the same time as the addition of the binding agent.

15 . Process according to claim 6 , wherein the burnout material comprises an organic material, preferably cellulose.

16 . Process according to claim 6 , wherein 1-30 wt.-%, of burnout material, relative to the dry weight of the suspension, is added.

17 . Process according to claim 6 , wherein the catalyst composition comprises particles having a particle size with a d 50 value of 2 to 10 μm.

18 . Process according to claim 6 , characterized in that the suspension is kept at a pH<7.

19 . Process according to claim 6 , wherein the binding agent comprises a sol, preferably a sol comprising Al 2 O 3 or ZrO 2 nanoparticles.

20 . Catalyst suspension, comprising a catalyst for methane steam reforming and a binding agent, characterized in that the suspension additionally contains a burnout material.

21 . Catalyst suspension according to claim 20 , wherein the suspension contains 1-30 wt.-%, burnout material, relative to the dry weight of the suspension.

22 . Catalyst suspension according to claim 20 , wherein the burnout material comprises an organic material, preferably cellulose.

23 . Catalyst suspension according to claim 20 , characterized in that the binding agent comprises a sol, preferably a sol comprising Al 2 O 3 or ZrO 2 nanoparticles.

24 . (canceled)

25 . Process of claim 6 further comprising burning out the burnout material.

26 . (canceled)

27 . Process according to claim 25 , wherein the calcining is carried out at 250-450° C.

28 . Process according to claim 25 , wherein the catalyst suspension is coated onto a carrier before the burning out.

29 . Process according to claim 28 , wherein the carrier comprises porous material, preferably an Ni foam.

30 . Process according to claim 28 , wherein the carrier has a metal surface.

31 . (canceled)

32 . (canceled)

33 . (canceled)

34 . (canceled)

Assignments (5)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 26, 2012
From: SUD-CHEMIE AG
To: CLARIANT PRODUKTE (DEUTSCHLAND) GMBH
Reel/Frame 029347/0116 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 31, 2009
From: WURTENBERGER, UWE
To: MTU ONSITE ENERGY GMBH
Reel/Frame 023169/0965 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 31, 2009
From: SUD-CHEMIE AG
To: MTU ONSITE ENERGY GMBH
Reel/Frame 023169/0993 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 31, 2009
From: MTU ONSITE ENERGY GMBH
To: SUD-CHEMIE AG
Reel/Frame 023170/0148 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 31, 2009
From: SPEYER, THOMAS; GABRIEL, WOLFGANG; WANNINGER, KLAUS
To: SUD-CHEMIE AG
Reel/Frame 023188/0547 →