Composite carbon molecular sieve membranes having anti-substructure collapse particles loaded in a core thereof

Patent metadata

Field	Value
Publication number	US-10086337-B2
Application number	US-201514827064-A
Country	US
Kind code	B2
Filing date	Aug 14, 2015
Priority date	Nov 30, 2014
Publication date	Oct 2, 2018
Grant date	Oct 2, 2018

Abstract

A carbon molecular sieve (CMS) membrane is made by pyrolyzing, to a peak pyrolysis temperature T P , a hollow fiber membrane having a polymeric sheath surrounding a polymeric core, anti-substructure collapse particles present in pores formed in the polymeric core help prevent collapse of pores formed in the hollow fiber membrane before pyrolysis. The anti-substructure collapse particles are made of a material or materials that either: i) have a glass transition temperature T G higher than T P , ii) have a melting point higher than T P , or ii) are completely thermally decomposed during said pyrolysis step at a temperature less than T P . The anti-substructure collapse particles are not soluble in a solvent used for dissolution of the polymeric material of the core.

First claim

What is claimed is:

1. A method for producing a CMS membrane fiber, comprising the steps of:
forming a composite precursor polymeric hollow fiber having a sheath covering a hollow core, the core being solidified from a core composition comprising essentially consisting of a polymeric core material dissolved in a core solvent or solvents, and silica particles insoluble in the core solvent or solvents, and optionally a pore former, the silica particles being disposed within pores formed in the polymeric core material, the sheath being solidified from a sheath composition comprising a polymeric sheath material dissolved in a sheath solvent, the silica particles having an average size of less than one micron, wherein there are no silica particles in the sheath; and
pyrolyzing the composite precursor polymeric hollow fiber up to a peak pyrolysis temperature TP, wherein the silica particles have a melting point higher than TP, wherein the core polymeric material is made of 6FDA:BPDA/DAM and the sheath polymeric material is made of 6FDA:BPDA/DAM.

2. The method of claim 1 , wherein a wt % of the polymer or copolymer in the core composition is lower than a wt % of the polymer or copolymer in the sheath composition.

3. The method of claim 1 , wherein a wt % of the silica particles in the core composition is selected such that the polymeric sheath material shrinks along a length of the fiber no more than +/−15% than that of the polymeric core material, but in any case is at least 5 wt %.

4. A CMS membrane fiber produced according to the method of claim 1 .

5. A CMS membrane module including a plurality of the CMS membrane fibers of claim 4 .

6. A method for separating a gas mixture, comprising the steps of feeding a gas mixture to the CMS membrane module of claim 5 , withdrawing a permeate gas from the CMS membrane module that is enriched in at least one gas relative to the gas mixture, and withdrawing a non-permeate gas from the CMS membrane module that is deficient in said at least one gas relative to the gas mixture.

Assignees

• Air Liquide
• Air Liquide

Inventors

• Kratzer Dean W
• Kosuri Madhava R
• Ma Canghai

Classifications

• Y02C20/40

  of CO2 · CPC title

• B01D2323/18

  Pore-control agents or pore formers · CPC title

• B01D69/088

  Co-extrusion; Co-spinning · CPC title

• B01D67/0067 Primary

  by carbonisation or pyrolysis · CPC title

• B01D53/228

  characterised by specific membranes · CPC title