Membranes for separation of carbon dioxide
View Patent ↗Methods for separating carbon dioxide from a fluid stream at a temperature higher than about 200° C. with selectivity higher than Knudsen diffusion selectivity include contacting a porous membrane with the fluid stream to preferentially transport carbon dioxide. The porous membrane includes a porous support and a continuous porous separation layer disposed on a surface of the porous support and extending between the fluid stream and the porous support layer. The porous support comprises alumina, silica, zirconia, stabilized zirconia, stainless steel, titanium, nickel-based alloys, aluminum-based alloys, zirconium-based alloys or a combination thereof. Median pore size of the porous separation layer is less than about 10 nm, and the porous separation layer comprises titania, MgO, CaO, SrO, BaO, La 2 O 3 , CeO 2 , HfO 2 , Y 2 O 3 , VO z , NbO z , TaO z , ATiO 3 , AZrO 3 , AAl 2 O 4 , A 1 FeO 3 , A 1 MnO 3 , A 1 CoO 3 , A 1 NiO 3 , A 2 HfO 3 , A 3 CeO 3 , Li 2 ZrO 3 , Li 2 SiO 3 , Li 2 TiO 3 , Li 2 HfO 3 , A 4 N 1 y O z , Y x N 1 y O z , La x N 1 y O z , HfN 2 y O z , or a combination thereof; wherein A is La, Mg, Ca, Sr or Ba; A 1 is La, Ca, Sr or Ba; A 2 is Ca, Sr or Ba; A 3 is Sr or Ba; A 4 is Mg, Ca, Sr, Ba, Ti or Zr; N 1 is V, Nb, Ta, Cr, Mo, W, Mn, Si or Ge; N 2 is V, Mo, W or Si; x is 1 or 2; y ranges from 1 to 3; and z ranges from 2 to 7.
1. A method for separating carbon dioxide from a fluid stream comprising carbon dioxide and hydrogen with selectivity higher than Knudsen diffusion selectivity, said method comprising contacting a porous membrane with the fluid stream at a temperature greater than about 200° C., the porous membrane comprising a porous support and a continuous porous separation layer disposed on a surface of the porous support and extending between the fluid stream and the porous support layer;
wherein the porous support comprises alumina, silica, zirconia, stabilized zirconia, stainless steel, titanium, nickel-based alloys, aluminum-based alloys, zirconium-based alloys or a combination thereof;
the porous separation layer comprises titania, MgO, CaO, SrO, BaO, La 2 O 3 , CeO 2 , HfO 2 , Y 2 O 3 , VO z , NbO z , TaO z , ATiO 3 , AZrO 3 , AAl 2 O 4 , A 1 FeO 3 , A 1 MnO 3 , A 1 CoO 3 , A 1 NiO 3 , A 2 HfO 3 , A 3 CeO 3 , Li 2 ZrO 3 , Li 2 SiO 3 , Li 2 TiO 3 , Li 2 HfO 3 , A 4 N 1 y O z , Y x N 1 y O z , La x N 1 y O z , HfN 2 y O z , or a combination thereof;
median pore size of the porous separation layer is less than about 10 nm; and
A is La, Mg, Ca, Sr or Ba;
A 1 is La, Ca, Sr or Ba;
A 2 is Ca, Sr or Ba;
A 3 is Sr or Ba;
A 4 is Mg, Ca, Sr, Ba, Ti or Zr;
N 1 is V, Nb, Ta, Cr, Mo, W, Mn, Si or Ge;
N 2 is V, Mo, W or Si;
x is 1 or 2;
y ranges from 1 to 3; and
z ranges from 2 to 7.
2. A method according to claim 1 , wherein the porous separation layer comprises titania.
3. A method according to claim 2 , wherein the titania of the porous separation layer comprises amorphous, anatase, metastable phases, or a combination thereof.
4. A method according to claim 1 , wherein the porous membrane comprises an intermediate layer disposed between the porous support and the continuous porous separation layer.
5. A method according to claim 4 , wherein the intermediate layer comprises alumina.
6. A method according to claim 1 , wherein the porous support comprises alumina.
7. A method according to claim 1 , wherein median pore size of the porous separation layer is less than about 5 nm.
8. A method according to claim 1 , wherein thickness of the porous separation layer is less than about 500 nm.
9. A method according to claim 1 , wherein thickness of the porous separation layer is less than about 300 nm.
10. A method according to claim 1 , wherein thickness of the porous separation layer is less than about 100 nm.
11. A method according to claim 1 , wherein CO 2 permeance of the porous membrane is greater than 10 −8 mol/m 2 /Pa/s at 200° C.
12. A method according to claim 1 , wherein CO 2 permeance of the porous membrane is greater than 10 −7 mol/m 2 /Pa/s at 200° C.
13. A method for separating carbon dioxide from a fluid stream comprising carbon dioxide and hydrogen, with selectivity higher than Knudsen diffusion selectivity, said method comprising contacting a porous membrane with the fluid stream at a temperature greater than about 200° C., the porous membrane prepared by a process comprising
combining at least one titanium alkoxide with water under acid conditions to form a titania sol; and
coating the titania sol on a surface of a porous support to form a continuous supported porous titania layer;
wherein the porous support comprises alumina, silica, zirconia, stabilized zirconia, stainless steel, titanium, nickel based alloys, aluminum-based alloys, zirconium-based alloys or a combination thereof.
14. A method according to claim 13 , wherein at least one template is additionally combined with the at least one titanium alkoxide to form the titania sol.
15. A method according to claim 14 , wherein the template is an ammonium halide.
16. A method according to claim 14 , wherein the template is tetrapropylammonium bromide.
17. A method according to claim 14 , wherein fractal dimension of the titania sol is less than about 2.0.
18. A method according to claim 13 , wherein fractal dimension of the titania sol is greater than about 2.0.
19. A method according to claim 13 , wherein the titania layer comprises amorphous, anatase, metastable phases, or a combination thereof.
20. A method according to claim 13 , wherein median pore size of the titania layer is less than about 5 nm.