Separation of carbon dioxide from ammonia
First Claim
1. THE METHOD OF REMOVING CARBON DIOXIDE FROM A MIXTURE OF AMMONIA AND CARBON DIOXIDE IN WHICH THE CARBON DIOXIDE IS PRESENT THEREIN IN AN AMOUNT IN EXCESS OF 2 PARTS PER MILLION BY VOLUME BUT NOT GREATER THAN 5/ PARTS PER MILLION BY VOLUME, WHICH COMPRISES PASSING SAID GAS MIXTURE THROUGH A MOLECULAR SIEVE COMPRISING A BED OF ACTIVATED ZEOLITE HAVING VOIDS WHOSE NARROWEST DIMENSION IS AT LEAST 4 ANGSTROM UNITS IN LENGTH TO PREFERENTIALLY ADSORB THE CARBON DIOXIDE, CONTINUING ADSORPTION UNTIL THE CARBON DIOXIDE, CONTINUING ADSORPTION UNHEATING THE ZEOLITE BED BY INDIRECT HEATING MEANS IN ADDITION TO A COUNTERCURRENT FLOW OF A PORTION OF THE PURIFIED AMMONIA WHICH HAS BEEN HEATED TO REGENERATE THE ZEOLITIC ADSORBENT BED, THEREAFTER COOLING THE ADSORBENT BED WITH A COOL CARBON DIOXIDE-FREE AMMONIA GAS.
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1 Claim
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1. THE METHOD OF REMOVING CARBON DIOXIDE FROM A MIXTURE OF AMMONIA AND CARBON DIOXIDE IN WHICH THE CARBON DIOXIDE IS PRESENT THEREIN IN AN AMOUNT IN EXCESS OF 2 PARTS PER MILLION BY VOLUME BUT NOT GREATER THAN 5/ PARTS PER MILLION BY VOLUME, WHICH COMPRISES PASSING SAID GAS MIXTURE THROUGH A MOLECULAR SIEVE COMPRISING A BED OF ACTIVATED ZEOLITE HAVING VOIDS WHOSE NARROWEST DIMENSION IS AT LEAST 4 ANGSTROM UNITS IN LENGTH TO PREFERENTIALLY ADSORB THE CARBON DIOXIDE, CONTINUING ADSORPTION UNTIL THE CARBON DIOXIDE, CONTINUING ADSORPTION UNHEATING THE ZEOLITE BED BY INDIRECT HEATING MEANS IN ADDITION TO A COUNTERCURRENT FLOW OF A PORTION OF THE PURIFIED AMMONIA WHICH HAS BEEN HEATED TO REGENERATE THE ZEOLITIC ADSORBENT BED, THEREAFTER COOLING THE ADSORBENT BED WITH A COOL CARBON DIOXIDE-FREE AMMONIA GAS.
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