Gas separator apparatus

1. An apparatus for separating at least one component from a mixture of a plurality of chemical species, the apparatus comprising:

a membrane structure comprising a plurality of pores disposed within a matrix material to allow mass transport from a first surface of the membrane structure to a second surface of the membrane structure, wherein the matrix material comprises a metal selected from the group consisting of nickel, stainless steel, iron-based alloy, nickel-based alloy, NiCrAlY, titanium, aluminum-based alloy, and copper-based alloy, wherein the matrix material has a thermal conductivity of greater than or equal to 10 W/m/K; and a functional material disposed within at least a portion of the plurality of pores, wherein the functional material has the property of promoting selective transport of at least one species through the membrane structure from the first surface to the second surface, wherein the functional material comprises a ceramic selected from the group consisting of magnesia, calcium oxide, strontium oxide, barium oxide, lanthanum oxide, ceria, titania, hafnia, yttria, vanadium oxide, niobium oxide, tantalum oxide, 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 , and HfN 2 y O z ,

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 is in the range from 1 to 3; and

z is in the range from 2 to 7.

2. The apparatus of claim 1 , wherein the metal comprises stainless steel.

3. The apparatus of claim 1 , wherein the matrix has a porosity volume fraction greater than about 5%.

4. The apparatus of claim 1 , wherein the matrix has a porosity volume fraction in a range from about 20% to about 70%.

5. The apparatus of claim 1 , wherein the matrix has a median pore size in the range from about 0.02 micrometers to about 200 micrometers.

6. The apparatus of claim 1 , wherein the matrix has a median pore size in the range from about 0.1 micrometer to about 10 micrometer.

7. The apparatus of claim 1 , wherein the matrix has a thickness in the range from about 50 micrometers to about 10 millimeters.

8. The apparatus of claim 1 , wherein the matrix has a thickness in the range from about 250 micrometers to about 5 millimeters.

9. The apparatus of claim 1 , wherein the functional material promotes selective transport of CO 2 through the membrane structure from the first surface to the second surface.

10. An apparatus for separating at least one component from a mixture of a plurality of chemical species, the apparatus comprising:

a metal membrane structure comprising a plurality of pores to allow heat transport from a first surface of the membrane structure to a second surface of the membrane structure, wherein the metal membrane structure comprises a metal selected from the group consisting of nickel, stainless steel, iron-based alloy, nickel-based alloy, NiCrAlY, titanium, aluminum-based alloy, and copper-based alloy; and

a functional material disposed within at least a portion of the plurality of pores, wherein the functional material has the property of promoting selective transport of CO 2 through the membrane structure from the first surface to the second surface, wherein the functional material comprises a ceramic selected from the group consisting of magnesia, calcium oxide, strontium oxide, barium oxide, lanthanum oxide, ceria, titania, hafnia, yttria, vanadium oxide, niobium oxide, tantalum oxide, 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 , and HfN 2 y O z ,

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 is in the range from 1 to 3; and

z is in the range from 2 to 7.

11. An apparatus for separating at least one component from a mixture of a plurality of chemical species, the apparatus comprising:

a membrane structure comprising a plurality of pores disposed within a matrix material to allow mass transport from a first surface of the membrane structure to a second surface of the membrane structure, wherein the matrix material has a thermal conductivity of at least 10 W/m/K; wherein the matrix material comprises a metal selected from the group consisting of nickel, stainless steel, iron-based alloy, nickel-based alloy, NiCrAlY, titanium, aluminum-based alloy, and copper-based alloy, and a functional material disposed within at least a portion of the plurality of pores within the metal, wherein the functional material has the property of promoting selective transport of at least one species through the membrane structure from the first surface to the second surface, wherein the functional material comprises an ionogel, or polynorbornene.

12. An apparatus for separating at least one component from a mixture of a plurality of chemical species, the apparatus comprising:

a metal membrane structure comprising a plurality of pores to allow heat transport from a first surface of the membrane structure to a second surface of the membrane structure; and

a functional material disposed within at least a portion of the plurality of pores within the metal of the membrane structure, wherein the functional material has the property of promoting selective transport of CO 2 through the membrane structure from the first surface to the second surface, wherein the functional material has the property of promoting selective transport of at least one species through the membrane structure from the first surface to the second surface, wherein the functional material comprises an ionogel, or polynorbornene.