Method and device for transferring gas molecules from a gaseous medium into a liquid medium or vice versa

Patent metadata

Field	Value
Publication number	US-9901885-B2
Application number	US-201314653428-A
Country	US
Kind code	B2
Filing date	Dec 18, 2013
Priority date	Dec 18, 2012
Publication date	Feb 27, 2018
Grant date	Feb 27, 2018

Abstract

The present invention relates. to methods and devices for exchanging gas molecules between a gaseous medium and a liquid medium which are particularly suited for applications such as blood oxygenation in heart-lung machines and gas scrubbing. The method of the invention comprises the following steps: a) providing a liquid medium having a surface tension in the range of from 0.02 N/m to 0.06 N/m, b) providing a gaseous medium, c) providing a membrane on an interface between the liquid medium and the gaseous medium, wherein the membrane comprises i) a carrier substrate with through-going openings having a mean diameter in the range from 0.2 μιη to 200 μπι, and ii) a porous superamphiphobic coating layer with openings having a mean diameter in the range from 0.1 μm to 10 μm, which is provided at least on the substrate surface facing the liquid medium, wherein either the liquid medium or the gaseous medium, preferably the gaseous medium, comprises at least one target gas to be transferred and said membrane is permeable for the at least one gas to be transferred and not permeable for the liquid medium due to the super-amphiphobic properties of the membrane surface facing the liquid medium with respect to said liquid medium, d) contacting the gaseous medium with the liquid medium via said superamphiphobic layer for a sufficient time to enrich the liquid or gaseous target medium with the at least one gas to be transferred.

First claim

The invention claimed is:

1. A method for transferring gas molecules from a gaseous medium into a liquid medium or vice versa comprising at least the following steps:
a) providing a liquid medium having a surface tension (liquid-air) in a range of from 0.02 N/m to 0.06 N/m,
b) providing a gaseous medium,
c) providing a membrane on an interface between the liquid medium and the gaseous medium, wherein the membrane comprises
i) a carrier substrate with through-going openings having a mean diameter in a range from 0.2 μm to 200 μm, and
ii) a porous superamphiphobic coating layer with openings having a mean diameter in a range from 0.1 μm to 10 μm, which coating layer comprises a surface exhibiting a contact angle of at least 150° with respect to 10 μl sized drops of water and also a contact angle of at least 150° with respect to 10 μl sized drops of liquids having a surface tension of not more than 0.06 N/m, which is provided at least on a substrate surface facing the liquid medium,
wherein either the liquid medium or the gaseous medium, comprises at least one target gas to be transferred and said membrane is permeable for the at least one gas to be transferred and not permeable for the liquid medium due to the superamphiphobic properties of the membrane surface facing the liquid medium with respect to said liquid medium,
d) contacting the gaseous medium with the liquid medium via said superamphiphobic layer for a sufficient time to enrich the liquid or gaseous target medium with the at least one gas to be transferred.

2. The method according to claim 1 , wherein gas molecules are transferred from a gaseous medium into a liquid medium.

3. The method according to claim 1 , wherein the at least one gas to be transferred is a member selected from the group consisting of oxygen, carbon dioxide, TiCl 4 , nitrogen oxides, SO 2 , SO 3 , H 2 S, HCl, HCN, ammonia, amines, and silanes.

4. A device for transferring gas molecules and/or particles from a gaseous medium into a liquid medium or vice versa comprising:
a) a liquid medium having a surface tension (liquid-air) in a range of 0.02 N/m to 0.06 N/m,
b) a gaseous medium,
c) a membrane provided on an interface between the liquid medium and the gaseous medium, wherein the membrane comprises
i) a carrier substrate with through-going openings having a mean diameter in a range from 0.2 μm to 200 μm, and
ii) a porous superamphiphobic coating layer with openings having a mean diameter in a range from 0.1 μm to 10 μm, which coating layer comprises a surface having a contact angle of at least 150° with respect to 10 μl sized drops of water and also a contact angle of at least 150° with respect to 10 μl sized drops of liquids having a surface tension of not more than 0.06 N/m, which is provided at least on the substrate surface facing the liquid medium,
which membrane is permeable for at least one gas contained in the liquid or gaseous medium, and not permeable for the liquid medium due to the superamphiphobic properties of the membrane surface facing the liquid medium with respect to said liquid medium.

5. The device according to claim 4 which is a gas scrubber or an oxygenator of a heart-lung machine or a component thereof.

6. The device according to claim 4 , wherein the superamphiphobic coating layer comprises strings, particles embedded in fibers, columns, aggregates or an arrangement of nano- or microparticles having a mean diameter in a range of 12 nm to 2 μm, which particles comprise a material of low surface energy or are coated with a material of low surface energy, wherein the low surface energy material has a surface tension (air-substrate surface) less than 0.03 N/m.

7. The device according to claim 4 , wherein the carrier substrate comprises a mesh, fibers, a textile, a micro- or mesoporous foam or a porous 3-dimensional structure with a defined shape.

8. The device according to claim 7 , wherein the porous 3-dimensional structure with a defined shape comprises an elongated longitudinally extended hollow body having at least one lumen or cavity provided in an interior thereof.

9. The device according to claim 4 , wherein the membrane comprises a carrier substrate with a microporous or mesoporous superamphiphobic layer provided on at least one substrate surface and wherein said porous layer is partially filled with the gaseous medium.

10. The device according to claim 4 , wherein the liquid medium exerts a hydrostatic pressure of at least 100 Pa, onto the superamphiphobic layer of the membrane.

11. The method according to claim 1 , wherein the liquid medium comprises blood, the gaseous medium is oxygen or an oxygen-containing gas mixture and the at least one gas to be transferred from the gaseous medium is oxygen.

12. The device according to claim 4 , wherein the membrane is produced by providing a carrier substrate with through-going openings having a mean diameter in a range from 0.2 μm to 200 μm, depositing particles having a mean diameter in a range of from 12 nm to 2 μm on the substrate surface, and, optionally, coating the particles with a hydrophobic top coating.

13. The device according to claim 12 , wherein the particles are polymer particles, silica particles or particles coated with a shell selected from the group consisting of a silica shell, a metal oxide shell, a Ti{OCH(CH 3 ) 2 } 4 shell, and a hybrid shell comprising 2 or more materials, wherein the silica particles or particles coated with a shell are further coated with a hydrophobic top coating.

14. The method according to claim 1 , wherein the method is used for gas scrubbing, flue gas desulfurization, silane capturing, or for medical treatment.

15. The method according to claim 1 , wherein the superamphiphobic coating layer comprises strings, particles embedded in fibers, columns, aggregates or an arrangement of nano- or microparticles having a mean diameter in a range of 12 nm to 2 μm, which particles comprise a material of low surface energy or are coated with a material of low surface energy, wherein the low surface energy material has a surface tension (air-substrate surface) less than 0.03 N/m.

16. The method according to claim 1 , wherein the carrier substrate comprises a mesh, fibers, a textile, a micro- or mesoporous foam or a porous 3-dimensional structure with a defined shape.

17. The method according to claim 1 , wherein the membrane comprises a carrier substrate with a microporous or mesoporous superamphiphobic layer provided on at least one substrate surface and wherein said porous layer is partially filled with the gaseous medium.

18. The method according to claim 1 , wherein the liquid medium exerts a hydrostatic pressure of at least 100 Pa, onto the superamphiphobic layer of the membrane.

19. The method according to claim 1 , wherein the membrane is produced by providing a carrier substrate with through-going openings having a mean diameter in a range from 0.2 μm to 200 μm, depositing particles having a mean diameter in a range of from 12 nm to 2 μm on the substrate surface, and, optionally, coating the particles with a hydrophobic top coating.

20. The method according to claim 19 , wherein the particles are polymer particles, silica particles or particles coated with a shell selected from the group consisting of a silica shell, a metal oxide shell, a Ti{OCH(CH 3 ) 2 } 4 shell, and a hybrid shell comprising 2 or more materials, wherein the silica particles or particles coated with a shell are further coated with a hydrophobic top coating.

Assignees

• Max Planck Gesellschaft

Inventors

• Butt Hans Juergen
• Vollmer Doris
• Deng Xu
• Paven Maxime
• Papadopoulos Periklis
• Mammen Lena

Classifications

• B01F3/04262

  Operations & Transport · mapped topic

• B01D2325/02

  Details relating to pores or porosity of the membranes · CPC title

• A61M1/32

  Oxygenators without membranes · CPC title

• B01F3/04269 Primary

  Operations & Transport · mapped topic

• B01D69/02

  characterised by their properties · CPC title