Reinforced capillary membranes and process for manufacturing thereof

• US 7,861,869 B2
• Filed: 11/18/2005
• Issued: 01/04/2011
• Est. Priority Date: 11/19/2004
• Status: Expired due to Fees

• Current Assignee: Vlaamse Instelling Voor Technologisch Onderzoek Nv (Vito Nv)
• Original Assignee: Vlaamse Instelling Voor Technologisch Onderzoek Nv (Vito Nv)
• Inventors: Doyen, Willy, Beckers, Herman, Dotremont, Chris
• Primary Examiner(s): Fortuna; Ana M
• Application Number:
  US11/791,133
• Publication Number:
  US 20080241451A1
• Time in Patent Office: 1,873 Days
• Field of Search: 210/490, 210/500.36, 210/500.41, 210/500.27, 210/500.38, 210/500.3, 210/500.23, 210/500.42, 264/41, 264/45.81, 264/172.16, 264/171.26, 264/171.27, 427/247, 428/376
• US Class Current: 210/490
• CPC Class Codes: B01D 2325/40 Fibre reinforced membranes
• CPC Class Codes: B01D 67/0011 Casting solutions therefor
• CPC Class Codes: B01D 67/0016 Coagulation
• CPC Class Codes: B01D 69/02 characterised by their properties
• CPC Class Codes: B01D 69/08 Hollow fibre membranes manufacture of hollow fibres D01D5/24, D01F1/08
• CPC Class Codes: B01D 69/10 Supported membranes; Membrane supports
• CPC Class Codes: B01D 69/107 Organic support material
• CPC Class Codes: Y10T 428/2935 Discontinuous or tubular or cellular core

Abstract

A process for manufacturing asymmetric braid reinforced capillary ultra- or micro-filtration membranes (1), including the subsequent steps of pulling a tubular braid (5) through a spinneret (7) and coating the braid with a dope. Prior to the coating step, the braid is impregnated with a non-coagulation liquid, being a liquid which does not cause coagulation of the dope, when brought in contact with the dope. The result is a membrane with an outer skin, i.e. smaller pores near the outside diameter than near the inside diameter, and a coating which is closely arranged around the outside diameter of the braid, without any substantial penetration of the coating into the braid.

Claims

1. A process for manufacturing asymmetric braid reinforced capillary ultra- or micro-filtration membranes, comprising the subsequent steps of pulling a tubular braid of monofilament yarn through a spinneret and coating the braid with a dope, wherein prior to said coating step, the braid is impregnated with a non-coagulation liquid, being a liquid which does not cause coagulation of said dope, when brought in contact with said dope wherein the membranes have a pure water flux at 20 degree C. of at least 4500 l/h.M2.bars.

2. The process according to claim 1, wherein the viscosity of said non-coagulation liquid lies between 0.01 and 5 Pa.s.

3. The process according to claim 1, wherein the internal channel of said tubular braid is filled completely by said non-coagulation liquid.

4. The process of claim 1, further comprising the steps of a controlled vapour phase followed by coagulation of the dope in a water bath having a temperature in the range of 40°

C. to 80°

C., further washing out of solvent and water soluble additives and drying.

5. The process of claim 1, further comprising the steps of coagulation in a mixture of non-solvent and solvent, followed by washing and drying.

6. The process according to claim 1 wherein the non-coagulation liquid comprises a solvent and a substance which lends a thixotropic behaviour to the liquid.

7. The process according to claim 1 wherein the non-coagulation liquid is a solution of a solvent, a viscosity increasing substance, and optionally a non-solvent in a concentration below the point where coagulation of the dope starts.

8. The process of claim 7 wherein said viscosity increasing substance comprises a water soluble polymer.

9. The process of claim 8, wherein the water soluble polymer is one or more of:

polyvinyl pyrrolidone (PVP) or polyethylene glycol (PEG) and an inorganic hydrophilic salt.

10. The process of claim 9, wherein the inorganic hydrophilic salt is LiCl.

11. The process as in claim 1, wherein the dope comprises organic solvent, polymer resin and hydrophilic compound.

12. The process as in claim 11, wherein said organic solvent is selected from the group consisting of N-methyl pyrrolidone, dimethyl formamide, dimethyl acetamide or a mixture thereof.

13. The process as in claim 11, wherein said polymer resin is selected from the group consisting of polysulphone, polyethersulfone, polyvinylidenedifluoride (PVDF), polyacronitrile, polyvinylchloride, polyimide, polyamideimide and polyesterimide.

14. The process as in claim 11, wherein said hydrophilic compound is selected from the group consisting of polyethylene glycol (PEG), polyvinylpyrrolidone (PVP), glycerol or a mixture thereof.

15. The process according to claim 1, wherein the braid material is selected from the group consisting of polyamide 6/6, polyamide 12, polypropylene, polyethylene, aramid and polyester.

16. A capillary membrane, produced according to the process of claim 1, comprising a tubular braid of monofilament yarn, and a polymer coating arranged around said braid, said coating having internal pores with a pore size that is smaller at the outside diameter of the coating and increases towards the inside diameter, characterized in that said coating is arranged in close contact with said braid, so that the inside surface of the coating follows every irregularity of the braid'"'"'s outside surface, without any substantial penetration of said coating into said braid wherein the membrane have a pure water flux at 20 degree C. of at least 4500 l/h.M2.bars.