US2013177824A1PendingUtilityA1

Systems and processes of operating fuel cell systems

Assignee: SHELL OIL COPriority: Jun 16, 2009Filed: Dec 18, 2012Published: Jul 11, 2013
Est. expiryJun 16, 2029(~2.9 yrs left)· nominal 20-yr term from priority
Y02E60/50H01M 8/04H01M 8/14H01M 8/06H01M 8/0618H01M 2008/147H01M 8/0662
60
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Claims

Abstract

The present invention is directed to systems and processes for operating molten carbonate fuel cell systems. A process for operating the molten carbonate fuel cell includes providing a hydrogen-containing stream comprising molecular hydrogen to a molten carbonate fuel cell anode; heating a hydrocarbon stream, at least a majority of which is comprised of hydrocarbons that are liquid at 20° C. and atmospheric pressure, with a heat source comprising an anode exhaust from the molten carbonate fuel cell anode; contacting at least a portion of the heated hydrocarbon stream with a catalyst to produce a steam reforming feed comprising gaseous hydrocarbons, hydrogen, and at least one carbon oxide; separating at least a portion of the molecular hydrogen from the steam reforming feed; and providing at least a portion of the separated molecular hydrogen to the molten carbonate fuel cell anode as at least a portion of the stream comprising molecular hydrogen.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
         1 . A process of operating a molten carbonate fuel cell, including a molten carbonate fuel cell anode, a molten carbonate fuel cell cathode, and having interposed there-between an electrolyte layer, wherein the process comprises:
 providing a hydrogen-containing stream comprising molecular hydrogen, to the molten carbonate fuel cell anode;   heating a hydrocarbon stream, at least a majority of which is comprised of hydrocarbons that are liquid at 20° C. and atmospheric pressure, with a heat source comprising an anode exhaust from the molten carbonate fuel cell anode to yield a heated hydrocarbon stream;   contacting at least a portion of the heated hydrocarbon stream with a catalyst to produce a steam reforming feed comprising, hydrogen and at least one carbon oxide;   separating at least a portion of the molecular hydrogen from the steam reforming feed to provide a separated hydrogen stream and an oxidant-containing gas stream; and   providing at least a portion of the separated hydrogen stream to the molten carbonate fuel cell anode as at least a portion of the hydrogen-containing stream.   
     
     
         2 . The process of  claim 1 , wherein the hydrocarbon stream comprises at least one hydrocarbon having a carbon number of from 4 to 25. 
     
     
         3 . The process of  claim 1 , wherein the hydrocarbon stream comprises diesel hydrocarbons. 
     
     
         4 . The process of  claim 1 , wherein the separated hydrogen stream contains at least about 0.6 mole fraction molecular hydrogen. 
     
     
         5 . The process of  claim 1 , further comprising contacting at least a portion of the steam forming feed with a second reforming catalyst to produce a reformed product gas comprising molecular hydrogen and carbon dioxide; separating the molecular hydrogen from the reformed product gas; and providing the thus-separated molecular hydrogen to the molten carbonate fuel cell anode as at least a portion of the hydrogen-containing stream. 
     
     
         6 . The process of  claim 1 , further comprising contacting at least a portion of the steam reforming feed with a second reforming catalyst to produce a reformed product gas comprising molecular hydrogen and carbon dioxide; separating the carbon dioxide from the reformed product gas and providing the thus-separated carbon dioxide to the molten carbonate fuel cell cathode. 
     
     
         7 . The process of  claim 1 , wherein the molecular hydrogen and water provided to the molten carbonate fuel cell anode is at a rate such that a molar ratio of water to molecular hydrogen in the anode stream is at most 1.0. 
     
     
         8 . The process of  claim 1 , further comprising the steps of: passing the oxidant-containing gas stream to an oxidizing unit, wherein the oxidant-containing gas stream comprises one or more gaseous hydrocarbons and at least one carbon oxide; contacting within the oxidizing unit at least a portion of the oxidant containing gas stream with an oxidant to thereby produce a second hydrogen-containing stream comprising hydrogen; and providing at least a portion of the second hydrogen-containing stream to the molten carbonate fuel cell anode. 
     
     
         9 . The process of  claim 1 , wherein the molten carbonate fuel cell generates electricity at an electrical power density of at least 0.1 W/cm 2 .

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