Amine-appended metal-organic frameworks exhibiting a new adsorption mechanism for carbon dioxide separations
An adsorption material is disclosed that comprises a metal-organic framework and a plurality of ligands. The metal-organic framework comprising a plurality of metal ions. Each respective ligand in the plurality of ligands is amine appended to a respective metal ion in the plurality of metal ions of the metal-organic framework. Each respective ligand in the plurality of ligands comprises a substituted 1,3-propanediamine. The adsorbent has a CO 2 adsorption capacity of greater than 2.50 mmol/g at 150 mbar CO 2 at 40° C. Moreover, the adsorbent is configured to regenerate at less than 120° C. An example ligand is diamine 2,2-dimethyl-1,3-propanediamine. An example of the metal-organic framework is Mg 2 (dobpdc), where dobpdc 4− is 4,4′-dioxidobiphenyl-3,3′-dicarboxylate. Example applications for the adsorption material are removal of carbon dioxide from flue gas and biogasses.
1. An adsorption material, comprising:
a metal-organic framework comprising a plurality of divalent cations and a plurality of
polytopic organic linkers; and
a plurality of ligands, wherein each respective ligand in the plurality of ligands is amine appended to a divalent cation in the plurality of divalent cations of the metal-organic framework, each respective ligand in the plurality of ligands comprising a substituted 1,3-propanediamine, wherein
the adsorption material has a CO 2 adsorption capacity of greater than 2.50 mmol/g at a total CO 2 partial pressure of 150 mbar, at 40° C., and
the adsorption material is configured to regenerate at less than 120° C.
2. An adsorption material comprising:
a metal-organic framework comprising a plurality of divalent cations and a plurality of
polytopic organic linkers; and
a plurality of ligands, wherein each respective ligand in the plurality of ligands is amine appended to a divalent cation in the plurality of divalent cations of the metal-organic framework,
wherein each respective ligand in the plurality of ligands has the structure:
wherein,
X labels an amine of the respective ligand that is appended to a divalent cation in the plurality of divalent cations,
Z is carbon, silicon, or germanium, and
R 1 , R 2 , R 3 , R 4 , R 5 , and R 6 are each independently selected from H, halogen, substituted or unsubstituted alkyl, substituted or unsubstituted heteroalkyl, substituted or unsubstituted aryl, substituted or unsubstituted heteroaryl, or substituted or unsubstituted heterocycloalkyl, with the provisos that
when R 3 is H, R 4 is other than H or methyl, and
when R 4 is H, R 3 is other than H or methyl,
wherein
the adsorption material has a CO 2 adsorption capacity of greater than 2.50 mmol/g at a total CO 2 partial pressure of 150 mbar, at 40° C., and
the adsorption material is configured to regenerate at less than 120° C.
3. The adsorption material of claim 2 , wherein one of R 3 and R 4 is H and the other of R 3 and R 4 is a substituted or unsubstituted alkyl.
4. The adsorption material of claim 2 , wherein R 1 , R 2 , R 3 , R 4 , R 5 , and R 6 are each independently H, halogen, substituted or unsubstituted n-alkyl or a substituted or unsubstituted branched-chain alkyl.
5. The adsorption material of claim 2 , wherein Z is carbon.
6. The adsorption material of claim 2 , wherein
the metal-organic framework comprises M 2 (dobpdc),
each M is a divalent cation in the plurality of cations and is in the group consisting of Mg, Ca, Mn, Cr, Fe, Co, Ni, Cu, and Zn,
each dobpdc is a polytopic organic linker in the plurality of polytopic organic linkers and has the composition 4,4′-dioxidobiphenyl-3,3′-dicarboxylate,
Z is carbon, and
R 3 and R 4 are each methyl.
7. An adsorption material comprising:
a metal-organic framework comprising a plurality of divalent cations and a plurality of
polytopic organic linkers; and
a plurality of ligands, wherein each respective ligand in the plurality of ligands is amine appended to a divalent cation in the plurality of divalent cations of the metal-organic framework, wherein each respective ligand in the plurality of ligands has the structure:
wherein
X labels an amine of the respective ligand that is appended to a divalent cation in the plurality of divalent cations,
Z 1 , is carbon, silicon, or germanium,
Z 2 , Z 3 , and Z 4 , are each independently carbon, silicon, germanium, sulfur or selenium,
R 1 , R 2 , R 3 , and R 4 , are each independently selected from H, halogen, substituted or unsubstituted alkyl, substituted or unsubstituted heteroalkyl, substituted or unsubstituted aryl, substituted or unsubstituted heteroaryl, or substituted or unsubstituted heterocycloalkyl, and
R 5 , R 6 , R 7 , R 8 , R 9 and R 10 are each independently selected from H, halogen, methyl, substituted methyl, ethyl, or substituted ethyl, with the provisos that
when Z 2 is sulfur or selenium, R 5 and R 6 are not present,
when Z 3 is sulfur or selenium, R 7 and R 8 are not present, and
when Z 4 is sulfur or selenium, R 9 and R 10 are not present,
wherein
the adsorption material has a CO 2 adsorption capacity of greater than 2.50 mmol/g at a total CO 2 partial pressure of 150 mbar, at 40° C., and
the adsorption material is configured to regenerate at less than 120° C.
8. The adsorption material of claim 7 , wherein Z 1 , Z 2 , Z 3 , and Z 4 , are each carbon.
9. The adsorption material of claim 7 , wherein R 1 , R 2 , R 3 , and R 4 are each independently H, halogen, substituted or unsubstituted n-alkyl or a substituted or unsubstituted branched-chain alkyl.
10. The adsorption material of claim 1 wherein each divalent cation in the plurality of divalent cations is Mg, Ca, Mn, Cr, Fe, Co, Ni, Cu, or Zn.
11. The adsorption material of claim 1 , wherein each polytopic organic linker in the plurality of polytopic organic linkers is 4,4′-dioxidobiphenyl-3,3′-dicarboxylate (dobpdc 4− ).
12. The adsorption material of claim 1 , wherein each polytopic organic linker in the plurality of polytopic organic linkers is:
4,4″-dioxido-[1,1′:4′,1″-terphenyl]-3,3″-dicarboxylate (dotpdc 4− ),
2,5-dioxidobenzene-1,4-dicarboxylate (dobdc 4− ),
3,3′ dioxide-biphenyl-4,4′-dicarboxylate (para-carboxylate-dobpdc 4− ),
1,3,5-benzenetristetrazolate (BTT),
1,3,5-benzenetristriazolate (BTTri),
1,3,5-benzenetrispyrazolate (BTP), or
1,3,5-benzenetriscarboxylate (BTC).
13. The adsorption material of claim 1 , wherein
each divalent cation in the plurality of divalent cations is Mg, Ca, Mn, Cr, Fe, Co, Ni, Cu, or Zn, and
each polytopic organic linker in the plurality of polytopic organic linker is 4,4′-dioxidobiphenyl-3,3′-dicarboxylate (dobpdc 4− ).
14. The adsorption material of claim 1 , wherein the metal-organic framework is a framework selected from the group of frameworks consisting of
(a) M-BTT, wherein
each M is a divalent cation in the plurality of cations and is in the group consisting of Ca, Fe, Mn, Cu, Co, Ni, Cr, and Cd, and
each BTT is a polytopic organic linker in the plurality of polytopic organic linkers and has the composition 1,3,5-benzenetristetrazolate, and
(b) Q-BTTri, wherein
each Q is a divalent cation in the plurality of cations and is in the group consisting of Cr, Mn, Fe, Co, Ni, and Cu, and
each BTTri is a polytopic organic linker in the plurality of polytopic organic linkers and has the composition 1,3,5-benzenetristriazolate.
15. The adsorption material of claim 1 , wherein the metal-organic framework is a framework selected from the group of frameworks consisting of
(a) M-BTP, wherein
each M is a divalent cation in the plurality of cations and is in the group consisting of Co, Ni, and Zn, and
each BTP is a polytopic organic linker in the plurality of polytopic organic linkers and has the composition 1,3,5-benzenetrispyrazolate, and
(b) Q 3 (BTC) 2 , wherein
each Q is a divalent cation in the plurality of cations and is in the group consisting of Cu and Cr, and
each BTC is a polytopic organic linker in the plurality of polytopic organic linkers and has the composition 1,3,5-benzenetriscarboxylate.
16. The adsorption material of claim 1 , wherein
the metal-organic framework comprises M 2 (dobdc),
each M is a divalent cation in the plurality of cations and is in the group consisting of Mg, Ca, Mn, Cr, Fe, Co, Ni, Cu, or Zn, and
each dobdc 4− is a polytopic organic linker in the plurality of polytopic organic linkers and has the composition 2,5-dioxido-1,4-benzenedicarboxylate.
17. The adsorption material of claim 1 , wherein the metal-organic framework comprises open metal sites and ligand occupied metal sites.
18. The adsorption material of claim 1 , wherein each divalent cation in the plurality of divalent cations is Mg.
19. The adsorption material of claim 1 , wherein the differential entropy of CO 2 adsorption of the adsorption material is less than −175 J/mol·K.
20. The adsorption material of claim 1 , wherein exposure of the adsorption material to CO 2 results in the formation of carbamic acid pairs between adjacent ligands in the plurality of ligands in the adsorption material.
21. The adsorption material of claim 1 , wherein the adsorption material has a CO 2 adsorption capacity of less than 3.00 mmol/g at 150 mbar CO 2 at 40° C.
22. The adsorption material of claim 1 , wherein the adsorption material has a working capacity of greater than of 2.3 mmol/g over less than a 70° C. temperature differential for CO 2 .
23. The adsorption material of claim 1 , wherein
the adsorption material has a Brunauer-Emmett-Teller (BET) surface area of at least 920 m 2 /g.
24. A method for abating CO 2 from a flue gas, the method comprising:
(a) contacting the flue gas with the adsorption material of claim 1 to reversibly adsorb CO 2 from the flue gas thereby generating an adsorption material enriched for CO 2 ; and
(b) thermally stripping a major portion of the CO 2 from the adsorption material enriched for CO 2 using a regeneration process.
25. A method of separating carbon dioxide produced by a source, comprising exposing the carbon dioxide from the source to the adsorption material of claim 1 , wherein the carbon dioxide is reversibly separated into the adsorption material by the method.
26. A method for removing CO 2 from a multi-component gas mixture comprising CO 2 and at least one of N 2 , H 2 O, and O 2 , the method comprising:
contacting the multi-component gas mixture with the adsorption material of claim 1 to reversibly adsorb CO 2 from the multi-component gas mixture thereby generating an adsorption material enriched for CO 2 and a residual gas that is depleted of CO 2 .