Porous polypropylene membrane and methods for production thereof

• US 5,139,529 A
• Filed: 08/25/1989
• Issued: 08/18/1992
• Est. Priority Date: 01/20/1987
• Status: Expired due to Term

• Current Assignee: Terumo Kabushiki Kaisha
• Original Assignee: Terumo Kabushiki Kaisha
• Inventors: Tatebe, Ken, Kido, Kousuke, Seita, Yukio, Nagaki, Shoichi
• Primary Examiner(s): Isabella, David
• Assistant Examiner(s): Gualtieri, G.
• Application Number:
  US07/392,988
• Time in Patent Office: 1,089 Days
• Field of Search: 210/500.21, 210/500.23, 210/500.27, 210/500.36, 264/41, 623/12, 623/66, 623/1
• US Class Current: 29/469.5
• CPC Class Codes: B01D 2323/21 Fillers
• CPC Class Codes: B01D 2325/02 Details relating to pores or porosity of the membranes
• CPC Class Codes: B01D 2325/0283 Pore size
• CPC Class Codes: B01D 67/003 by selective elimination of components, e.g. by leaching
• 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 71/26 Polyalkenes
• CPC Class Codes: B01D 71/262 Polypropylene
• CPC Class Codes: D01D 5/24 with a hollow structure; Spinnerette packs therefor D01D5/38 takes precedence; producing tubes of plastic material B29D; addition of agents forming hollow filaments D01F1/08
• CPC Class Codes: D01F 6/06 from polypropylene
• CPC Class Codes: Y10T 29/49906 Metal deforming with nonmetallic bonding

Abstract

A porous polypropylene hollow fiber membrane is disclosed which is characterized by the fact that the solid phase in the inner surface region thereof is formed with particles of polypropylene closely fused and joined to give rise to a continuous phase while partially exposed through the surface thereof, the solid phase in the interior and the outer surface region thereof is formed with particles of polypropylene interconnected in the direction of axis of fiber to give rise to a multiplicity of lumps of polypropylene, and the interstices between these solid phases has continuous pores interconnected in the form of a three-dimensional network. When this porous polypropylene hollow fiber membrane is used in an artificial lung, without reference to the choice between the type adapted to pass blood inside the hollow fiber membrane, it exhibits a high gas-exchange capacity without infliction of injury upon blood cells, aggravation of pressure loss, or leakage of blood plasma. Further a flat-film type porous polypropylene membrane possessing a microreticular structure is disclosed which is characterized by the fact that either or both of the opposite surface region of the porous membrane forms a surface layer possessing practically the same micro-reticular structure as in the interior of said membrane and said membrane possesses an average pore diameter in the range of 0.1 to 5.0 μm, a bubble point of not more than 2.0 kgf/cm², a porosity in the range of 60 to 85%, a water permeability of not less than 100 ml/min.mmHg.m² and a wall thickness in the range of 30 to 300 μm. When this flat-film type porous polypropylene membrane is used for blood plasma separation, it effects the blood plasma separated at a high speed and sparingly entails occlusion of blood cells or hemolysis.

Claims

1. A method for the production of a porous polypropylene hollow fiber membrane, comprising:

mixing polypropylene, an organic filler, and a crystalline seed forming agent to form a resultant mixture wherein said organic filler is uniformly dispersed in said polypropylene in a molten state and readily soluble in an extractant,

discharging the resultant mixture in a molten state through annular spinning orifices,

cooling and solidifying the resultant hollow threads by contact with a cooling and solidifying liquid having no compatibility with said organic filler and possessing a specific heat capacity in the range of 0.2 to 0.7 cal/g, wherein the cooling and solidifying liquid is silicone oil or polyethylene glycol, and

bringing the cooled and solidified hollow threads into contact with an extractant incapable of dissolving polypropylene, thereby removing said organic filler therefrom by extraction.

2. A method according to claim 1, wherein liquid paraffin is used as the organic filler.

3. A method according to claim 1, wherein the proportion of said organic filler to 100 parts by weight of said polypropylene is in the range of 35 to 150 parts by weight.

4. A method according to claim 1, wherein said crystalline seed forming agent is an organic heat-resistant substance possessing a melting point of not less tan 150°

C. and a gelling point of not less than the crystallization starting point of the polypropylene being used.

5. A method according to claim 1, wherein the proportion of said crystalline seed forming agent to 100 parts by weight of said polypropylene is in the range of 0.1 to 5 parts by weight.

6. A method according to claim 1, wherein said silicone oil possesses a viscosity in the range of 2 to 50 centistokes at 20°

C.