High capacity carbon dioxide sorbent
The present invention provides a sorbent for the removal of carbon dioxide from gas streams, comprising: a CO 2 capacity of at least 9 weight percent when measured at 22° C. and 1 atmosphere; an H 2 O capacity of at most 15 weight percent when measured at 25° C. and 1 atmosphere; and an isosteric heat of adsorption of from 5 to 8.5 kilocalories per mole of CO 2 . The invention also provides a carbon sorbent in a powder, a granular or a pellet form for the removal of carbon dioxide from gas streams, comprising: a carbon content of at least 90 weight percent; a nitrogen content of at least 1 weight percent; an oxygen content of at most 3 weight percent; a BET surface area from 50 to 2600 m 2 /g; and a DFT micropore volume from 0.04 to 0.8 cc/g.
1. A carbon sorbent for the removal of carbon dioxide from gas streams, comprising:
(a) a CO 2 capacity of at least 9 weight percent when measured at 22° C. and 1 atmosphere;
(b) an H 2 O capacity of at most 1 weight percent when measured at 25° C. and 1 atmosphere;
(c) an isosteric heat of adsorption of from 6 to 8.5 kilocalories per mole of CO 2 ; and,
(d) a nitrogen content of at least 2.2 wt %, which is present in the form of pyridine, pyridone or pyrrole.
2. The carbon sorbent of claim 1 , wherein the isosteric heat of adsorption is from 6.0 to 7.7 kilocalories per mole of CO 2 .
3. The carbon sorbent of claim 1 further comprising: a CO 2 capacity of at least 7 weight percent when measured at 60° C. and 1 atmosphere.
4. The carbon sorbent of claim 1 further comprising: a CO 2 capacity of at least 4.8 weight percent when measured at 22° C. and 0.15 atmosphere.
5. The carbon sorbent of claim 1 further comprising: a CO 2 capacity of at least 2.3 weight percent when measured at 60° C. and 0.15 atmosphere.
6. A carbon sorbent in a powder, a granular or a pellet form for the removal of carbon dioxide from gas streams, comprising:
(a) a carbon content of at least 90 weight percent;
(b) a nitrogen content of at least 2.2 weight percent, which is present in the form of pyridine, pyridone or pyrrole;
(c) an oxygen content of at most 1.8 weight percent;
(d) a BET surface area from 50 to 2600 m 2 /g; and,
(e) a DFT micropore volume from 0.04 to 0.8 cc/g.
7. The carbon sorbent of claim 6 , further comprising: an H 2 O capacity of at most 1 weight percent, based on the mass of the sorbent when measured at 25° C. and 1 atmosphere.
8. The carbon sorbent of claim 6 , further comprising: an isosteric heat of adsorption of from 6.0 to 8.5 kilocalories per mole of CO 2 .
9. The carbon sorbent of claim 8 , wherein the isosteric heat of adsorption is from 6.0 to 7.7 kilocalories per mole of CO 2 .
10. The carbon sorbent of claim 6 , further comprising: a carbon dioxide capacity of at least 9 weight percent when measured at 1.0 atmosphere and 22° C.
11. The carbon sorbent of claim 6 , further comprising: a carbon dioxide capacity of at least 4.8 weight percent when measured at 0.15 atmosphere and 22° C.
12. The carbon sorbent of claim 6 , further comprising: a carbon dioxide capacity of at least 7 weight percent when measured at 1.0 atmosphere and 60° C.
13. The carbon sorbent of claim 6 , further comprising: a carbon dioxide capacity of at least 2.3 weight percent when measured at 0.15 atmosphere and 60° C.
14. The carbon sorbent of claim 6 , further comprising: a pH of at least 9.0.
15. The carbon sorbent of claim 14 , further comprising: a pH of at least 11.0.