Polyamine phosphorus dendrimer materials for carbon dioxide capture
The present disclosure provides novel solid sorbents synthesized by the reaction of polyamines with polyaldehyde phosphorous dendrimer (P-dendrimer) compounds. The sorbents are highly stable and exhibit rapid reaction kinetics with carbon dioxide, making the sorbents applicable for carbon capture, and can be easily regenerated for further use. The material is stable to aqueous and organic media, as well as strong acid and bases. The sorbent maintains full capacity over extended use. The material can be used for CO 2 capture from pure CO 2 streams, mixed gas streams, simulated flue gas, and ambient air. Additionally, the material can be adhered to surfaces for reversible CO 2 capture applications outside of bulk particle-based processes.
1. A polyamine phosphorus dendrimer (P-dendrimer) having the formula I
wherein W is a phosphorus based dendrimer core; X is a polyfunctional aromatic linker; Y may be present or absent and if present is a polyfunctional amino phosphoryl group linked to a polyfunctional aromatic linker; Z is an diamino alkyl group, a polyalkyl amino group, a polyethyleneimine, or a polypropyleneimine; j and k are numerical values corresponding to the branch point multiplicity and whose values independently range from 1 to 10; and 1 is a numerical value corresponding to the branch point multiplicity and whose values ranges from 2 to 10.
2. The P-dendrimer of claim 1 , wherein
W is a phosphazene, thiophosphoryl, or a cyclophosphazatetraene group;
X is
wherein Nu is —OH, —SH, or —NH 2 ; each R 1 is independently —CHO, —CN, —COOMe, COOEt, COOH, CH 2 OH, CONH 2 , or COCH 3 ; each R 2 is independently H, Me, Et or halogen;
Y is
Z is
and each n or m if present is independently an integer from 1-6.
3. The polyamine P-dendrimer of claim 1 , having a CO 2 capacity of greater than 2 weight percent.
4. The polyamine P-dendrimer of claim 1 , having a CO 2 capacity of greater than 5 weight percent.
5. The polyamine P-dendrimer of claim 1 , having a CO 2 capacity of greater than 10 weight percent.
6. A composite material which comprises a solid support and a surface coated with the polyamine P-dendrimer of claim 1 having Formula I.
7. The composite material of claim 5 , wherein the solid support is a polymeric material, carbon, glass, or a metal support.
8. The composite material of claim 6 , wherein the polymeric material is natural or a synthetic polymer.
9. The composite material of claim 7 , wherein the natural polymer is a cellulose acetate, a silk protein, a soy protein, or a starch.
10. The composite material of claim 7 , wherein the synthetic polymer is petroleum pitch, polyacrylonitrile, polyamide, polyethylene, polypropylene, polystyrene, polyvinyl chloride or a mixture thereof.
11. A method of removing CO 2 from a gaseous fluid stream which comprises contacting the gaseous fluid stream with the polyamine P-dendrimer of claim 1 having Formula I.
12. A method of adsorbing, separating, storing or sequestering carbon dioxide (CO 2 ), comprising contacting the polyamine P-dendrimer of claim 1 having Formula I with a gaseous fluid stream comprising carbon dioxide (CO 2 ).
13. A method of removing CO 2 from a gaseous fluid stream which comprises contacting the gaseous fluid stream with a polyamine phosphorus dendrimer (P-dendrimer) having the formula I
at a temperature in the range of about 20° C. to about 90° C.;
wherein W is a phosphorus based dendrimer core; X is a polyfunctional aromatic linker; Y may be present or absent and if present is a polyfunctional amino phosphoryl group linked to a polyfunctional aromatic linker; Z is an diamino alkyl group, a polyalkyl amino group, a polyethyleneimine, or a polypropyleneimine; j and k are numerical values corresponding to the branch point multiplicity and whose values independently range from 1 to 10; and 1 is a numerical value corresponding to the branch point multiplicity and whose values ranges from 2 to 10.
14. The method of claim 13 , wherein the gaseous fluid stream is a flue gas.
15. The method of claim 14 , wherein the flue gas is flue gas from a natural gas power plant, a coal-fired power plant, a cement plant or other industrial process.
16. The method of claim 14 , wherein the flue gas stream has a CO 2 content of about 3 mole % to about 45 mole % CO 2 .
17. The method of claim 13 , wherein the gaseous fluid stream is a post-combustion stream.
18. The method of claim 13 , wherein the gaseous fluid stream is ambient air.
19. The method of claim 18 , wherein the gaseous fluid stream has a CO 2 content of about 350 to about 450 parts per million (PPM) CO 2 .
20. The method of claim 18 , wherein the gaseous fluid stream has a CO 2 content of about 450 to about 1000 parts per million (PPM) CO 2 .
21. The method of claim 18 , wherein the gaseous fluid stream has a CO 2 content of about 1000 to about 4000 parts per million (PPM) CO 2 .
22. The method of claim 13 , further comprising regenerating the polyamine P-dendrimer of formula I by heating the P-dendrimer to a temperature in the range of about 50° C. to about 150° C.
23. A process for the capture and removal of CO 2 from a CO 2 -containing stream the process comprising:
(a) providing a housing having dispersed therein a sorbent comprising the polyamine P-dendrimer of claim 1 ;
(b) passing a CO 2 -containing stream through the housing such that the CO 2 -containing stream contacts the sorbent;
(c) flushing the housing with steam to cause the sorbent to desorb an CO 2 retained therein as a result of contact of the sorbent with the CO 2 -containing stream; and
(d) flushing the housing with air to remove the steam from the housing.
24. A method of making a polyamine phosphorus dendrimer (P-dendrimer) having the formula I
wherein W is a phosphorus based dendrimer core; X is a polyfunctional aromatic linker; Y may be present or absent and if present is a polyfunctional amino phosphoryl group linked to a polyfunctional aromatic linker; Z is an diamino alkyl group, a polyalkyl amino group, a polyethyleneimine, or a polypropyleneimine; j and k are numerical values corresponding to the branch point multiplicity and whose values independently range from 1 to 10; and 1 is a numerical value corresponding to the branch point multiplicity and whose values ranges from 2 to 10;
which method comprises:
(a) reacting a phosphoryl chloride starting material for the phosphorus based dendrimer core with a nucleophilic aldehyde starting material for the polyfunctional aromatic linker so as to form a polyphosphoryl ester aldehyde compound;
(b) condensing the polyphosphoryl ester aldehyde compound with an polyalkyl amine to form a polyalkyl imine polyphosphoryl ester; and
(c) reducing the a polyalkyl imine polyphosphoryl ester to form the polyamine phosphorus dendrimer (P-dendrimer).