US2008076007A1PendingUtilityA1

Catalyst and a Method for Manufacturing the Same

Individually held — no corporate assignee on recordPriority: Apr 11, 2002Filed: Oct 30, 2007Published: Mar 27, 2008
Est. expiryApr 11, 2022(expired)· nominal 20-yr term from priority
B01J 35/395B01J 2235/30B01J 35/30C25D 5/605C25D 5/627C25D 5/623Y02E60/50H01M 4/94H01M 4/92H01M 4/8853C25D 3/50Y02P70/50B01J 23/42B01J 23/44H01M 4/8807B01D 2255/1021H01M 4/921B01J 23/468B01D 53/945B01J 23/40C25D 21/12B01J 37/348H01M 4/90H01M 8/1007B01J 37/0215Y02T10/12H01M 8/00B01J 23/08
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Claims

Abstract

An improved platinum and method for manufacturing the improved platinum wherein the platinum having a fractal surface coating of platinum, platinum gray, with a increase in surface area of at least 5 times when compared to shiny platinum of the same geometry and also having improved resistance to physical stress when compared to platinum black having the same surface area. The process of electroplating the surface coating of platinum gray comprising plating at a moderate rate, for example at a rate that is faster than the rate necessary to produce shiny platinum and that is less than the rate necessary to produce platinum black. Platinum gray is applied to manufacture a fuel cell and a catalyst.

Claims

exact text as granted — not AI-modified
1 . An anode and/or a cathode comprising a substrate wherein the surface coating is electroplated to the surface of said conductive substrate at a rate such that the metal particles form on the conductive substrate faster than necessary to form shiny platinum and slower than necessary to form platinum black.  
     
     
         2 . A method for manufacturing of a catalyst by electroplating a surface coating such that surface has a rough surface coating comprising: 
 electroplating the surface of a conductive substrate at a rate such that the particles are form on the conductive substrate faster than necessary to form shiny platinum and slower than necessary to form platinum black.    
     
     
         3 . The method of  claim 2  wherein said step of electroplating is accomplished at a rate of more than 0.05 microns per minute, but less than 1 micron per minute.  
     
     
         4 . The method of  claim 2  wherein said electroplating is accomplished at a rate of greater or equal to 1 micron per minute, but less than 10 microns per minute.  
     
     
         5 . The method of  claim 2  wherein said electroplating is controlled by the electrode voltage.  
     
     
         6 . The method of  claim 5  wherein said voltage is a constant voltage.  
     
     
         7 . The method of  claim 5  wherein the controlled voltage causes at least a partially diffusion limited plating reaction.  
     
     
         8 . The method of  claim 2  wherein the voltage of said electroplating is less than 0.2 Volts and greater than −1 Volts vs. Ag/AgCl reference electrode.  
     
     
         9 . The method of  claim 2  wherein the electroplating solution is at least 3 mM but less than 30 mM ammonium hexachloroplatinate in about 0.4 M disodium hydrogen phosphate.  
     
     
         10 . A method of using at least one catalyst of  claim 1  in a fuel cell.  
     
     
         11 . A method of using at least one catalyst of  claim 1  in an autocatalyst.

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