Hollow fiber membrane tubesheets of variable epoxy composition and hardness

• US 6,290,756 B1
• Filed: 12/03/1997
• Issued: 09/18/2001
• Est. Priority Date: 12/03/1997
• Status: Expired due to Term

• Current Assignee: L'Air Liquide SA
• Original Assignee: Praxair Technology Incorporated (Linde Plc)
• Inventors: Ford, Cheryl Ann, Nelson, Joyce Katz, Macheras, James Timothy
• Primary Examiner(s): Fortuna, Ana
• Assistant Examiner(s): Ward, Richard W.
• Application Number:
  US08/984,633
• Time in Patent Office: 1,385 Days
• Field of Search: 96/8, 96/10, 210/500.23, 210/321.8, 210/321.89, 210/321.88, 210/321.87, 210/321.79, 210/321.61, 264/261, 264/279, 156/294, 428/217
• US Class Current: 96/8
• CPC Class Codes: B01D 53/22 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 Class Codes: B01D 63/022 Encapsulating hollow fibres
• CPC Class Codes: B01D 63/0221 using a mould
• CPC Class Codes: B01D 63/023 Encapsulating materials
• CPC Class Codes: B01D 63/024 with a single potted end

Abstract

Multicomponent hollow fiber membrane tubesheets are disclosed that provide for improved membrane performance, particularly at high operating pressures. The multicomponent tubesheets have an epoxy resin having, when cured, different degrees of hardness in different portions of the tubesheet. Methods for producing such multicomponent tubesheets are also provided.

Claims

1. A membrane separation module for the separation of gaseous components at high pressure, said module comprising,

a bundle of gas separation hollow fiber membranes, each of said membranes having at least one region which is encapsulated by a tubesheet, and an active membrane region which is not encapsulated by said tubesheet;

said tubesheet comprising a cured epoxy resin having, when cured, a comparatively soft epoxy portion and a comparatively hard epoxy portion within said tubesheet, said comparatively hard epoxy portion having a hardness at least 10 shore D units greater than said comparatively soft epoxy portion at a temperature of 25°

C.;

said comparatively soft epoxy portion being located at a first end defining an interface between the encapsulated region of said membranes and the active membrane region of said membranes, said comparatively soft epoxy portion being soft and flexible so as to protect the fibers from damage or sealing imperfections at said interface;

said comparatively hard portion being located at a terminal end of said tubesheet located opposite of said first end, said comparatively hard epoxy portion providing durability and mechanical support required for high pressure and temperature separation of gases; and

said comparatively hard epoxy portion being in intimate contact with said comparatively soft epoxy portion such that there are substantially no air gaps between said portions, so as to reduce the presence of tubesheet defects which may reduce the selectivity of a gas separation process conducted with said module.

2. The membrane separation module of claim 1, wherein a difference in hardness varies continuously between said first end and said terminal end.

3. The membrane separation module of claim 1 wherein said comparatively hard epoxy portion and said comparatively soft epoxy portion are formed from two distinct epoxy formulations.

4. The membrane separation module of claim 3, wherein a weight ratio of said comparatively hard epoxy portion to said comparatively soft epoxy portion is from about 1000:

1 to about 1;

10.

5. The membrane separation module of claim 3 wherein said comparatively soft epoxy portion either contains reactive or nonreactive diluents, or is formulated by the use of a stoichiometric excess of epoxy hardener, or both.

6. The membrane separation module of claim 5 wherein said comparatively soft epoxy portion contains said reactive or nonreactive diluents.

7. The membrane separation module of claim 5 wherein said comparatively soft epoxy portion is formulated by the use of a stoichiometric excess of an epoxy hardener.

8. The membrane separation module of claim 3 wherein said comparatively soft epoxy portion has an initial viscosity of about 1500 centipoise or less at 25°

C.

9. The membrane separation module of claim 1 wherein the said interface layer is formed by applying a hardness modifying agent on top of an uncured or partially cured hard epoxy formulation layer.

10. The membrane separation module of claim 9 wherein said hardness modifying agent is a reactive or nonreactive diluent.

11. The membrane separation module of claim 10 wherein said reactive diluent is a functional siloxane.

12. The membrane separation module of claim 11 wherein said functional siloxane is an aminofunctional siloxane.

13. The membrane separation module of claim 1, wherein said comparatively soft epoxy portion has a Shore D hardness of less than about 80 units.

14. The membrane separation module of claim 1, wherein said comparatively hard epoxy portion has a Shore D hardness of greater than about 80 units.

15. A process of forming a potted bundle of gas separation hollow fiber membranes for a gas separation module, said process comprising:

a) forming a layer of either a comparatively soft epoxy resin or a hardness modifying agent on top of a comparatively hard epoxy resin to form striated layers having a comparatively hard epoxy portion and a comparatively soft epoxy portion;

b) introducing an end of a gas separation hollow fiber membrane bundle into said striated layers of epoxy such that an end impregnated with said epoxy resins is formed;

c) curing said epoxy resins to form a multicomponent tubesheet;

wherein

said bundle of gas separation hollow fiber membranes has an active membrane region which is not encapsulated by said tubesheet;

said bundle and said tubesheet forming a potted bundle;

said tubesheet comprises a comparatively soft epoxy portion and a comparatively hard epoxy portion within said tubesheet, said comparatively hard epoxy portion having a hardness at least 10 shore D units greater than said comparatively soft epoxy portion at a temperature of 25°

C.;

said comparatively soft epoxy portion being located at a first end defining an interface between the encapsulated region of said membranes and the active membrane region of said membranes, said comparatively soft epoxy portion being soft and flexible so as to protect the fibers from damage or sealing imperfections at said interface;

said comparatively hard portion being located at a terminal end of said tubesheet located opposite of said first end, said comparatively hard epoxy portion providing mechanical support required for high pressure and temperature separation of gases; and

said comparatively hard epoxy portion being in intimate contact with said comparatively soft epoxy portion such that there are substantially no air gaps between said portions, so as to reduce the presence of tubesheet defects which may reduce the selectivity of a gas separation process conducted with said potted bundle.

16. The process of claim 15 further comprising the step of placing said end impregnated with said epoxy resins into a mold, and backfilling said mold with said soft epoxy resin prior to curing said epoxy resin layers.

17. A process of forming a potted bundle of gas separation hollow fiber membranes for a gas separation module, said process comprising:

potting an end of a bundle of gas separation hollow fiber membranes in a comparatively hard epoxy resin and applying a layer of either a comparatively soft epoxy resin or an epoxy resin hardness modifier above said end having said comparatively hard epoxy layer to form a tubesheet;

wherein

said bundle of gas separation hollow fiber membranes has an active membrane region which is not encapsulated by said tubesheet, said bundle and said tubesheet forming a potted bundle;

said tubesheet comprises a comparatively soft epoxy portion and a comparatively hard epoxy portion within said tubesheet, said comparatively hard epoxy portion having a hardness at least 10 shore D units greater than said comparatively soft epoxy portion at a temperature of 25°

C.;

said comparatively soft epoxy portion being located at a first end defining an interface between the encapsulated region of said membranes and the active membrane region of said membranes, said comparatively soft epoxy portion being soft and flexible so as to protect the fibers from damage or sealing imperfections at said interface;

said comparatively hard portion being located at a terminal end of said tubesheet located opposite of said first end, said comparatively hard epoxy portion providing mechanical support required for high pressure and temperature separation of gases; and

said comparatively hard epoxy portion being in intimate contact with said comparatively soft epoxy portion such that there are substantially no air gaps between said portions, so as to reduce the presence of tubesheet defects which may reduce the selectivity of a gas separation process conducted with said potted bundle.

18. A process of claim 17 wherein said comparatively hard epoxy layer is cured prior to introduction of said comparatively soft epoxy layer.

19. A process of claim 17 wherein said comparatively soft epoxy resin or epoxy resin hardness modifier is introduced through a central region of the bundle.

20. A process of claim 17 wherein said comparatively soft epoxy resin or epoxy resin hardness modifier is introduced from an exterior region of the bundle.