Woven membrane module with controlled tubesheet epoxy wicking

Patent metadata

Field	Value
Publication number	US-9283524-B2
Application number	US-201314136505-A
Country	US
Kind code	B2
Filing date	Dec 20, 2013
Priority date	Dec 20, 2013
Publication date	Mar 15, 2016
Grant date	Mar 15, 2016

Abstract

A gas separation membrane module is formed from a woven fabric of weft membrane hollow fibers and warp yarns. The membrane module includes an active hollow fiber region spanning the inner edges of the two tubesheets. The membrane module also includes two tubesheets formed by encapsulating membrane fiber on one or both ends. The tubesheet on the end includes a first sub-region adjacent the active fiber and a second sub-region extending from first sub-region to the outer face of the tubesheet. The spacing of the warp threads is relatively denser in the first sub-region than in the active region or the second sub-region.

First claim

What is claimed is:

1. A gas separation membrane module for separation of a gas mixture, comprising:
a core tube having an axis;
a fabric spirally wrapped around the core tube, the fabric comprising weft hollow fibers that are semi-permeable to the gas mixture and also warp threads, the weft hollow fibers extending in a direction parallel to the core axis, the warp threads spiraling in a direction perpendicular to the weft hollow fibers;
first and second tubesheets disposed at and impregnating opposite axial ends of the wrapped fabric, the tubesheets being comprised of thermoset or thermoplastic resin;
an active region being a first section of the fabric extending between the first and second tubesheets;
each second section of the fabric impregnated by one of the tubesheets comprising a first sub-region adjacent the active region and a second sub-region extending from the associated first sub-region to the associated axial end of the fabric, the warp threads being spaced more densely in each first sub-region than in each second sub-regions and the active region;
first and second end caps secured to a pressure vessel to completely encase the outer ends of the first and second tubesheets, at least one of the end caps including at least one first orifice for introduction or withdrawal of a gas; the pressure vessel encasing the first and second tubesheets, surrounding at least the active region and including at least one second orifice for introduction or withdrawal of a gas.

2. The module of claim 1 , further comprising first and second O-rings each of which is disposed in a groove formed in an outer surface of the first or second tubesheet adjacent the inner wall of the pressure vessel to provide a seal between the first or second tubesheet and the inner wall of the pressure vessel.

3. The module of claim 1 , wherein the active region and second sub-regions have a warp thread spacing of 0.1 cm to 5.0 cm and the first sub-regions have a warp thread spacing of 0.03 cm to 0.3 cm.

4. The module of claim 1 , wherein the thermoset or thermoplastic resin of the tubesheets is an epoxy resin.

5. The module of claim 1 , wherein the weft fibers are made of a polymeric material selected from the group consisting of polysulfones, polyether sulfones, polyimides, polyamides, and blends thereof.

6. A method of manufacturing the gas separation membrane module of claim 1 , comprising the steps of:
wrapping the fabric around the core tube;
injecting liquid, resinous potting composition comprising the thermoset or thermoplastic resin into a first end of the fabric-wrapped core for a time sufficient to impregnate the first and second sub-regions and fill in the potting composition among interstices of the weft fibers thereat;
allowing the liquid resin to cure and form an associated tubesheet;
injecting liquid, resinous potting composition into a second end of the fabric-wrapped core for a time sufficient to impregnate the first and second sub-regions and fill in the potting composition among the interstices of the weft fibers thereat;
allowing the liquid resin to cure and form the other associated tubesheet;
machining one or both outer ends of the tubesheets by removing the potting composition to open one or both ends of the weft hollow fibers on the outer ends of the tubesheet;
securing the endcaps to the pressure vessel to completely encase the tubesheets; and
securing the pressure vessel to encase the membrane bundle and tubesheets.

7. The method of claim 6 , further comprising the steps of machining a groove in an outer surface of each tubesheet and placing O-rings in the grooves to provide a gas tight seal between the tubesheets and the pressure vessels.

8. A method of using the gas separation membrane module of claim 1 where each of the end caps includes an orifice for introduction or withdrawal of a gas, comprising the steps of:
introducing a gas mixture to the orifice of one of the end caps;
withdrawing a permeate from the orifice of the pressure vessel; and
withdrawing a non-permeate from the orifice of the other of the end caps.

9. A method of using the gas separation membrane module of claim 1 where the pressure vessel includes at least one second orifice for introducing or withdrawing a gas, comprising the steps of:
introducing a gas mixture to one of the at least one second orifice of the pressure vessel;
withdrawing a permeate from the first orifice of one of the end caps; and
withdrawing a non-permeate from the first orifice of the other end cap.

10. A method of using the gas separation membrane module of claim 6 , wherein one ends of the weft hollow fibers are kept closed with the potting composition on the outer end of the first tubesheet and the other ends of the weft hollow fibers are machined by removing the potting composition to open on the outer end of the second tubesheet, each of the end caps includes at least one first orifice for introduction or withdrawal of a gas, comprising the steps of:
introducing a gas mixture to the second orifice of the pressure vessel;
withdrawing a permeate gas from the open ends of the weft hollow fibers to the first orifice of the end caps; and
withdrawing a non-permeate gas from the core tube to the closed ends of the weft hollow fibers and the first orifice of the other end cap, wherein the core tube is perforated.

Assignees

• Air Liquide
• L Air Liquide Société Anonyme Pour L Étude Et L Expl Des Procedes Georges Claude

Inventors

• Li Tao
• Sanders Jr Edgar S
• Bennett Michael D

Classifications

• B01D53/22

  by diffusion (manufacturing semi-permeable membranes B01D67/00; form, structure or properties of semi-permeable membranes B01D69/00; material for semi-permeable membranes B01D71/00) · CPC title

• B01D2053/224

  with hollow fibres · CPC title

• B01D63/026

  Wafer type modules or flat-surface type modules · CPC title

• B01D63/02 Primary

  Hollow fibre modules · CPC title

• B01D63/022

  Encapsulating hollow fibres · CPC title