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A process for the production of hydrogen and electrical energy, with zero emission of pollutants, from ethanol which is produced from biomass, which is characterized by the partial oxidation/reforming of ethanol with water for hydrogen production which is subsequently fed to a fuel cell for producti

A process for the production of hydrogen and electrical energy, with zero emission of pollutants, from ethanol which is produced from biomass, which is characterized by the partial oxidation/reforming of ethanol with water for hydrogen production which is subsequently fed to a fuel cell for production of electrical energy, more specifically where an aqueous solution of ethanol originating from fermentation of biomass is separated by distillation or any other technique so as to obtain approximately 40-70% by weight of ethanol, preferably 50-60%, this mixture, mixed with a suitable quantity of air in such a way so as the ratio of moles oxygen per mole ethanol to be between zero and 0.5, is fed to a reactor in which the reactions of partial oxidation and reforming of ethanol are taking place over a suitable catalyst, where in the same or a different reactor the shift reaction is taking place and, if necessary, the reaction of combustion of CO or its conversion to CH4,where the gaseous mixture from the exit of the reactors which contain hydrogen in mixture with carbon dioxide, nitrogen, methane or other gases in small quantities, is separated to the extent which is desirable for any kind of application.

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1. A method of producing hydrogen gas comprising: contacting a 40-70% by weight aqueous solution of ethanol with a Ni/La2O3catalyst under suitable conditions such that hydrogen gas and carbon dioxide are produced. 2. The method of claim 1 further comprising the step of: separating the hydrog

1. A method of producing hydrogen gas comprising: contacting a 40-70% by weight aqueous solution of ethanol with a Ni/La2O3catalyst under suitable conditions such that hydrogen gas and carbon dioxide are produced. 2. The method of claim 1 further comprising the step of: separating the hydrogen gas from the carbon dioxide. 3. The method of claim 1 wherein the suitable conditions include the application of heat. 4. The method of claim 1 wherein the suitable conditions include the introduction of oxygen or air. 5. A method of using a Ni/La2O3catalyst to produce hydrogen gas comprising: contacting an ethanol and water mixture with a Ni/La2O3catalyst and oxygen or air. 6. A method of producing electric energy comprising: a) fermenting biomass to produce an ethanol and water mixture; b) distilling the ethanol and water mixture to a concentration of 40-70% by weight of ethanol; c) contacting the distilled ethanol and water mixture with a Ni/La2O3catalyst and oxygen or air to produce hydrogen gas and carbon dioxide; d) converting residual carbon monoxide and water to carbon dioxide and hydrogen gas; e) separating the carbon dioxide from the hydrogen gas produced in steps (c) and/or (d); and f) feeding the hydrogen gas to a fuel cell to produce electrical energy. 7. A method of producing heat comprising: a) fermenting biomass to produce an ethanol and water mixture; b) distilling the ethanol and water mixture to a concentration of 40-70% by weight of ethanol; c) contacting the distilled ethanol and water mixture with a Ni/La2O3catalyst and oxygen or air to produce hydrogen gas and carbon dioxide; d) converting residual carbon monoxide and water to carbon dioxide and hydrogen gas; e) separating the carbon dioxide from the hydrogen gas produced in steps (c) and/or (d); and f) feeding the hydrogen gas to a fuel cell to produce heat. 8. The method of claim 6 or claim 7 wherein the fuel cell is of the phosphoric acid, proton exchange membrane, or solid polymer type. 9. The method of any of claims 5 and 6-7 wherein the ethanol and water mixture is 50-60% by weight of ethanol. 10. A composition comprising ethanol, water and Ni/La2O3catalyst. 11. A reactor containing an ethanol and water mixture in contact with a Ni/La2O3catalyst. 12. The reactor of claim 11 wherein the ethanol and water mixture is 40-70% by weight of ethanol. 13. The reactor of claim 11 wherein the ethanol and water mixture is 50-60% by weight of ethanol. 14. The reactor of claim 11 wherein the ethanol and water mixture is further in contact with air or oxygen. 15. The reactor of claim 11 wherein the ethanol and water mixture is further in contact with hydrogen gas and carbon dioxide.