Removal of hydrogen impurity from gas streams

Abstract

Trace hydrogen may be removed from a dry gas by passing the dry gas at a temperature from about 0°C to about 60°C through at least one layer of a first hopcalite catalyst to produce product gas that is at least substantially free of hydrogen, wherein the first hopcalite catalyst has a molar ratio of copper to manganese of more than 0.55. Advantages include increase hydrogen capacity, lower feed and regeneration temperatures and lower sensitivity to carbon dioxide than equivalent processes using standard hopcalite catalyst having a Cu / Mn molar ratio from 0.45 to 0.55.

Claims

A process for removing hydrogen from a dry gas comprising hydrogen as an impurity, said process comprising passing said dry gas at a temperature from 0°C to 60°C through at least one layer of a first hopcalite catalyst to produce product gas that is at least substantially free of hydrogen, wherein said first hopcalite catalyst has a molar ratio of copper to manganese of more than 0.55.The process according to Claim 1, wherein said molar ratio of copper to manganese in said first hopcalite catalyst is less than 7.The process according to Claim 1, wherein said molar ratio of copper to manganese in said first hopcalite catalyst is in a range from 0.6 to 4.The process according to Claim 1, wherein said molar ratio of copper to manganese in said first hopcalite catalyst is in a range from 2 to 4.The process according to Claim 1, wherein said molar ratio of copper to manganese in said first hopcalite catalyst is in a range from 0.6 to 1.

2. The process according to Claim 1, wherein said first hopcalite catalyst has a surface area of less than 280 m2 / g.The process according to Claim 1, wherein said first hopcalite catalyst has a surface area in a range from 100 m2 / g to 200 m2 / g.The process according to Claim 1, wherein said first hopcalite catalyst has a total pore volume of less than 0.4 cm3 / g.The process according to Claim 1, wherein said first hopcalite catalyst has a total pore volume in a range from 0.1 cm3 / g to 0.3 cm3 / g. The process according to Claim 1, wherein said hydrogen impurity is present in said dry gas in an amount of up to 40 ppmv.The process according to Claim 1, wherein said hydrogen impurity present in said dry gas in an amount of more than 20 ppmv.The process according to Claim 1, wherein said dry gas comprises carbon dioxide in an amount up to 900 ppmv.The process according to Claim 1, wherein said layer(s) of said first hopcalite catalyst is / are regenerated at a temperature below 200°C.The process according to Claim 1, wherein said layer(s) of said first hopcalite catalyst is / are regenerated at a temperature no more than 150°C.The process according to Claim 1, wherein said layer(s) of said first hopcalite catalyst is / are regenerated at a temperature no more than 80°C.The process according to Claim 1, wherein the temperature of said dry gas is in a range from 10°C to 15°C.The process according to Claim 1, wherein said dry gas is passed through said layer(s) of said first hopcalite catalyst at a pressure in a range from 3 bar to 45 bar (0.3 MPa to 4.5 MPa).The process according to Claim 1, said process comprising passing the dry gas through at least one layer of a second hopcalite catalyst upstream of said layer(s) of said first hopcalite catalyst, wherein said second hopcalite catalyst has a molar ratio of copper to manganese of no more than 0.

55. A process for removing hydrogen from dry air comprising said hydrogen as an impurity, said process comprising passing said dry air at a pressure from 3 bar to 45 bar (0.3 MPa to 4.5 MPa) and at a temperature from 0°C to 60°C through at least one layer of a first hopcalite catalyst to produce dry air that is at least substantially free of hydrogen, wherein said first hopcalite catalyst has a molar ratio of copper to manganese in a range from 2 to 4. A process for removing hydrogen and carbon monoxide from dry air comprising said hydrogen and said carbon monoxide as impurities, said process comprising passing said dry air at a pressure from 3 bar to 45 bar (0.3 MPa to 4.5 MPa) and at a temperature from 0°C to 60°C through at least one layer of a first hopcalite catalyst to produce dry air that is at least substantially free of hydrogen and carbon monoxide, wherein said first hopcalite catalyst has a molar ratio of copper to manganese in a range from 0.6 to 1.2.

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