IP Library Granted Patent US 9,242,210
Granted Patent B1
US 9,242,210 · App. 14/215,964 · Granted Jan 26, 2016

Enzymatically active high-flux selectively gas-permeable membranes

Inventors: Ying-Bing Jiang (Albuquerque, NM); Joseph L. Cecchi (Albuquerque, NM); Susan Rempe (Albuquerque, NM); Yaqin Fu (Albuquerque, NM); C. Jeffrey Brinker (Albuquerque, NM)
Assignees: STC.UNM; SANDIA CORPORATION
B01D53/62
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Quick Facts
Patent No.
US 9,242,210
App. No.
14/215,964
Granted
Jan 26, 2016
Kind
B1
Abstract

An ultra-thin, catalyzed liquid transport medium-based membrane structure fabricated with a porous supporting substrate may be used for separating an object species such as a carbon dioxide object species. Carbon dioxide flux through this membrane structures may be several orders of magnitude higher than traditional polymer membranes with a high selectivity to carbon dioxide. Other gases such as molecular oxygen, molecular hydrogen, and other species including non-gaseous species, for example ionic materials, may be separated using variations to the membrane discussed.

Claims (42)

1. A membrane structure for moving an object species from a first region having an object species first concentration, through the membrane structure, to a second region having a object species second concentration different from the first concentration, wherein the object species is a gaseous molecule or non-gas species to be selectively transported from the first region to the second region, the membrane structure comprising:

a supporting substrate comprising a plurality of pores therethrough;

a nanoporous layer within the plurality of pores, the nanoporous layer being thinner than the supporting substrate, wherein the nanoporous layer comprises:

a hydrophilic layer having a thickness of 50 nm or less; and

a hydrophobic layer; and

a liquid transport medium within the hydrophilic layer, wherein the liquid transport medium comprises:

a liquideous permeation medium; and

at least one catalyst within the liquideous permeation medium.

2. The membrane structure of claim 1 , wherein:

the plurality of pores have a first portion having a first average diameter at a first side of the supporting substrate adjacent to the first region;

the plurality of pores have a second portion having a second average diameter at a second side of the supporting substrate adjacent to the second region, wherein the first average diameter is smaller than the second average diameter; and

the nanoporous layer is within the first portion of the plurality of pores.

3. The membrane structure of claim 2 , wherein the second portion of the plurality of pores is free from the nanoporous layer.

4. The membrane structure of claim 2 , wherein:

the first average diameter is between about 2 nanometers (nm) and about 1000 nm; and

the second average diameter is between 0.5 μm and about 10 millimeters.

5. The membrane structure of claim 1 , wherein the supporting substrate comprises at least one of anodized porous alumina, silica, ceramic, a polymer, a metal, a metal alloy, a metallic composite material, and combinations of two or more of these.

6. The membrane structure of claim 1 , wherein the nanoporous layer comprises at least one of silica, silicate, a metal oxide, or a combination thereof.

7. The membrane structure of claim 1 , wherein the liquideous permeation medium comprises water and the catalyst is an enzyme comprising carbonic anhydrase.

8. The membrane structure of claim 7 , wherein the membrane structure is configured to move an object species comprising carbon dioxide.

9. The membrane structure of claim 1 , wherein the nanoporous layer has a thickness of between about 5 nanometers and about 100 micrometers and the hydrophilic layer has a thickness of about 2 nanometers to about 10 nanometers.

10. The membrane structure of claim 8 , wherein the supporting substrate has a thickness of between about 10 micrometers and about 200 micrometers.

11. The membrane structure of claim 1 , further comprising:

the plurality of pores have a first portion having a first average diameter at a first side of the supporting substrate;

the supporting substrate comprises at least one of anodized porous alumina, silica, ceramic, a polymer, a metal, a metal alloy, a metallic composite material, and combinations of two or more of these;

the plurality of pores have a second portion having a second average diameter at a second side of the supporting substrate, wherein the first average diameter is smaller than the second average diameter;

the nanoporous layer comprises at least one of a silica, silicate, metal oxide, or a combination thereof and is within the first portion of the plurality of pores;

the second portion of the plurality of pores is free from the nanoporous layer; and

the liquideous permeation medium comprises water and the catalyst is an enzyme comprising carbonic anhydrase.

12. A membrane structure for moving an object species from a first region having an object species first concentration, through the membrane structure, to a second region having an object species second concentration different from the first concentration, wherein the object species is a gaseous molecule or non-gas species to be selectively transported from the first region to the second region, the membrane structure comprising:

a supporting substrate comprising a plurality of pores therethrough;

a nanoporous layer within the plurality of pores, the nanoporous layer being thinner than the supporting substrate, wherein the nanoporous layer comprises:

a hydrophilic layer having a thickness of 50 nm or less and being configured to allow a liquid transport medium to be positioned within the first layer; and

a hydrophobic layer.

13. The membrane structure of claim 12 , wherein the supporting substrate comprises at least one of anodized porous alumina, silica, ceramic, a polymer, a metal, a metal alloy, a metallic composite material, and combinations of two or more of these.

14. The membrane structure of claim 13 , wherein the nanoporous layer comprises at least one of nanoporous silica, mesoporous silica, nanoporous polymeric material, nanoporous organic-inorganic composite, silicates, oxides, metals, metal alloys, carbon, sulfides and composites thereof.

15. The membrane structure of claim 12 , wherein the supporting substrate comprises at least one of anodized porous alumina, ceramic, a polymer, a metal, a metal alloy, a metallic composite material, and combinations of two or more of these.

16. The membrane structure of claim 15 , wherein the nanoporous layer comprises at least one of nanoporous silica, mesoporous silica, silicate, a metal oxide, or a combination thereof.

17. The membrane structure of claim 12 , wherein the nanoporous layer comprises nanoporous silica or mesoporous silica.

18. The membrane structure of claim 15 , wherein the supporting substrate comprises anodized porous alumina.

19. The membrane structure of claim 15 , wherein the supporting substrate comprises a polymer.

20. The membrane structure of claim 12 , wherein the hydrophilic layer has a thickness of about 2 nanometers to about 10 nanometers.

Assignments (6)
CONFIRMATORY LICENSE Recorded Nov 5, 2021
From: UNIVERSITY OF NEW MEXICO
To: UNITED STATES DEPARTMENT OF ENERGY
Reel/Frame 058795/0459 →
CHANGE OF NAME Recorded May 24, 2018
From: SANDIA CORPORATION
To: NATIONAL TECHNOLOGY & ENGINEERING SOLUTIONS OF SANDIA, LLC
Reel/Frame 046232/0273 →
CONFIRMATORY LICENSE Recorded Dec 29, 2015
From: SANDIA CORPORATION
To: U.S. DEPARTMENT OF ENERGY
Reel/Frame 037396/0121 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 10, 2015
From: REMPE, SUSAN
To: SANDIA CORPORATION
Reel/Frame 037259/0685 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 18, 2014
From: JIANG, YING-BING; FU, YAQIN; BRINKER, C. JEFFREY; CECCHI, JOSEPH L.
To: THE REGENTS OF THE UNIVERSITY OF NEW MEXICO
Reel/Frame 033125/0157 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 18, 2014
From: THE REGENTS OF THE UNIVERSITY OF NEW MEXICO
To: STC.UNM
Reel/Frame 033125/0167 →
Continuity (1)
Provisional Application 61786404 · Mar 15, 2013