초록 ▼

The present invention involves an improved adsorbent for gas separation processes. The adsorbent comprises a binary ion exchanged Type X zeolite wherein between 5% and 40% of the available ion sites are occupied by Ca, and between 60% and 95% of the available ion sites are occupied by Sr. The presen

The present invention involves an improved adsorbent for gas separation processes. The adsorbent comprises a binary ion exchanged Type X zeolite wherein between 5% and 40% of the available ion sites are occupied by Ca, and between 60% and 95% of the available ion sites are occupied by Sr. The present adsorbent is especially useful for the adsorption of N 2 from an air stream at superambient pressure to produce an O 2 -rich product stream.

대표청구항 ▼

1. A binary ion exchanged Type X zeolite adsorbent wherein between 5% and 40% of the available ion sites are occupied by Ca and between 60% and 95% of the available ion sites are occupied by Sr. 2. A binary ion exchanged Type X zeolite adsorbent in accordance with claim 1 wherein between 8% and 12%

1. A binary ion exchanged Type X zeolite adsorbent wherein between 5% and 40% of the available ion sites are occupied by Ca and between 60% and 95% of the available ion sites are occupied by Sr. 2. A binary ion exchanged Type X zeolite adsorbent in accordance with claim 1 wherein between 8% and 12% of the available ion sites are occupied by Ca. 3. A binary ion exchanged Type X zeolite adsorbent in accordance with claim 2 wherein between 88% and 92% of the available ion sites are occupied by Sr. 4. A binary ion exchanged Type X zeolite adsorbent in accordance with claim 1 wherein 0-5% of the ion sites are occupied by Na. 5. A process for producing an oxygen-enriched stream from a gas stream comprising nitrogen and oxygen, said process comprising: contacting said gas stream with a binary ion exchanged Type X zeolite adsorbent so as to adsorb a portion of the nitrogen present in said gas stream wherein between 5% and 40% of the available ion sites on the adsorbent are occupied by Ca and between 60% and 95% are occupied by Sr. 6. A process in accordance with claim 5 wherein said gas stream is contacted with a binary ion exchanged Type X zeolite adsorbent wherein between 8% and 12% of the available ion sites are occupied by Ca. 7. A process in accordance with claim 6 wherein said gas stream is contacted with a binary ion exchanged Type X zeolite adsorbent wherein between 88% and 92% of the available ion sites are occupied by Sr. 8. The process in accordance with claim 5 wherein the adsorbent bed is subsequently depressurized and purged with an oxygen-rich stream to regenerate the adsorbent bed and produce a nitrogen-rich stream. 9. A process for removing nitrogen from a gas stream comprising nitrogen and oxygen, said process comprising: a. establishing and maintaining said gas stream at a temperature between 0° and 50° C. and at a pressure between 1 atm and 5 atm; and b. passing said feed gas over an adsorbent bed comprising a binary ion exchanged Type X zeolite wherein between 5% and 40% of the available ion sites are occupied by Ca, and between 60% and 95% of the available ion sites are occupied by Sr, such that at least a portion of the nitrogen in said gas stream is adsorbed by the adsorbent bed, thereby leaving an oxygen-rich product stream. 10. The process in accordance with claim 9 wherein said adsorbent bed is initially pressurized to about 3.7 atm with an oxygen-enriched gas. 11. The process in accordance with claim 10 wherein said adsorbent bed is depressurized and subsequently back-purged with an oxygen-rich gas stream to remove part of the nitrogen, thereby regenerating the adsorbent bed.