Method and system for generating hydrogen-enriched fuel gas for emissions reduction and carbon dioxide for sequestration

Abstract

A method of generating hydrogen-enriched fuel gas and carbon dioxide comprising converting hydrocarbon molecules from a gaseous hydrocarbon feed stream into hydrogen and carbon dioxide, separating the hydrogen and carbon dioxide, blending the hydrogen back into the gaseous hydrocarbon feed stream to generate a hydrogen-enriched fuel gas, and utilizing the carbon dioxide for storage or sequestration. A system for generating hydrogen-enriched fuel gas and carbon dioxide comprising an inlet handling system, a syngas and water-gas shift system, a water-gas compression system, a carbon dioxide recovery system, a dehydration system, and a carbon dioxide compression system.

1 . A method of generating hydrogen-enriched fuel gas and carbon dioxide comprising:
 (a) converting hydrocarbon molecules from a gaseous hydrocarbon feed stream into hydrogen and carbon dioxide;   (b) separating the hydrogen and carbon dioxide;   (c) blending the hydrogen back into the gaseous hydrocarbon feed stream to generate a hydrogen-enriched fuel gas; and   (d) utilizing the carbon dioxide for storage or sequestration.   
     
     
         2 . The method of  claim 1 , wherein as a result of the separation step, each standard cubic foot of the gaseous hydrocarbon feed. stream produces between two and four standard cubic feet of a hydrogen product stream and between 0.7 and 0.9 standard cubic feet of a carbon dioxide product stream. 
     
     
         3 . The method of  claim 1 , wherein the hydrogen-enriched fuel gas has a hydrogen concentration ranging from five to 30 mole percent. 
     
     
         4 . The method of  claim 1 , wherein the hydrogen-enriched fuel gas produces less carbon dioxide per energy unit output when combusted than non-hydrogen-enriched natural gas. 
     
     
         5 . The method of  claim 1 , wherein approximately one to eleven percent of the gaseous hydrocarbon feed stream is processed. 
     
     
         6 . The method of  claim 1 , wherein the gaseous hydrocarbon feed stream has a total volume;
 wherein the total volume of the gaseous hydrocarbon feed stream ranges from 100 million standard cubic feet per day to 4500 million standard cubic feet per day; and   wherein between 10 million standard cubic feet per day and 500 million standard cubic feet per day of the gaseous hydrocarbon feed stream is processed.   
     
     
         7 . The method of  claim 1 , wherein there is an existing natural gas pipeline transportation and distribution system, and
 wherein the hydrogen-enriched fuel gas is transported and distributed using the existing natural gas pipeline system.   
     
     
         8 . The method of  claim 1 , wherein the sequestration is enhanced oil recovery. 
     
     
         9 . The method of  claim 1 , wherein the carbon dioxide is separated from the hydrogen using a carbon dioxide recovery solvent, and
 wherein the carbon dioxide recovery solvent is one or more hydrocarbon liquid(s) selected from the group consisting of butanes, pentanes, hexanes, heptanes, octanes, aromatics, and isomers of butanes, pentanes, hexanes, heptanes, octanes and aromatics.   
     
     
         10 . The method of  claim 1 , wherein a carbon dioxide recovery solvent is used to separate the carbon dioxide from the hydrogen; and
 wherein the carbon dioxide recovery solvent allows the carbon dioxide to be separated from the hydrogen at a pressure of between 200 and 500 psig.   
     
     
         11 . The method of  claim 10 , wherein total carbon dioxide compression requirements for the storage or sequestration are reduced by 50 to 75 percent as compared to chemical or physical solvent-based carbon dioxide recovery processes that do not utilize the carbon dioxide recovery solvent of the present invention. 
     
     
         12 . The method of  claim 1 , wherein the conversion, separation and blending steps occur on a natural gas transportation and distribution pipeline and not at a point of combustion. 
     
     
         13 . The method of  claim 1 , wherein the conversion, separation and blending steps are all performed prior to combustion of the hydrogen-enriched fuel gas. 
     
     
         14 . The method of  claim 1 , wherein there is an existing natural gas pipeline transportation and distribution system,
 wherein there are a number of existing compressed natural gas fueling facilities; and   wherein the conversion, separation and blending steps do not require any changes to the existing natural gas pipeline transportation and distribution system other than providing mobile points of consumption with an ability to consume the hydrogen-enriched fuel gas and increasing the number of compressed natural gas fueling facilities to supply the mobile points of consumption with the hydrogen-enriched fuel gas.   
     
     
         15 . The method of  claim 1 , further comprising:
 (e) utilizing a portion of the separated hydrogen as a separate fuel product.   
     
     
         16 . The method of  claim 1 , wherein the gaseous hydrocarbon feed stream is pipeline quality natural gas. 
     
     
         17 . A system for generating hydrogen-enriched fuel gas and carbon dioxide comprising:
 (a) means for converting hydrocarbon molecules from a gaseous hydrocarbon feed stream into hydrogen and carbon dioxide;   (b) means for separating the hydrogen and carbon dioxide;   (c) means for blending the hydrogen back into the gaseous hydrocarbon feed stream to generate a hydrogen-enriched fuel gas; and   (d) means for utilizing the carbon dioxide for storage or sequestration.   
     
     
         18 . A method of generating hydrogen and carbon dioxide comprising:
 (a) converting hydrocarbon molecules from a gaseous hydrocarbon feed stream into hydrogen and carbon dioxide;   (b) separating the hydrogen and carbon dioxide;   (c) utilizing the hydrogen as a separate product; and   (d) utilizing the carbon dioxide for storage or sequestration;   wherein the carbon dioxide is separated from the hydrogen using a carbon dioxide recovery solvent; and   wherein the carbon dioxide recovery solvent is one or more hydrocarbon liquid(s) selected from the group consisting of butanes, pentanes, hexanes, heptanes, octanes, aromatics, and isomers of butanes, pentanes, hexanes, heptanes, octanes and aromatics.   
     
     
         19 . The method of  claim 18 , wherein a carbon dioxide recovery solvent is used to separate the carbon dioxide from the hydrogen; and
 wherein the carbon dioxide recovery solvent allows the carbon dioxide to be separated from the hydrogen at a pressure of between 200 and 500 psig.