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(12) PATENT APPLICATION PUBLICATION<br />

(19) INDIA (21) Application No.: 00927/KOLNP/2005 A<br />

(22) Date <strong>of</strong> filing <strong>of</strong> Application: 18/05/2005 (43) Publication Date: 09/06/2006<br />

(54) Title <strong>of</strong> <strong>the</strong> invention: HYDROPHILIC MICROPOROUS MEMBRANE<br />

(51) International classification : B01D 61/04, 69/12,<br />

71/34, 71/78, C08J<br />

9/36<br />

(31) Priority Document No : 2002-304766<br />

2002-376767<br />

2003-023709<br />

(32) Priority Date : 18/10/2002<br />

26/12/2002<br />

31/01/2003<br />

(33) Name <strong>of</strong> priority country : JAPAN<br />

(86) International Application No and : PCT/JP03/13329 &<br />

Filing Date<br />

: 17/10/2003<br />

(87) International Publication No : WO 04/035180<br />

(61) Patent <strong>of</strong> addition to Application No : NA<br />

Filed on : NA<br />

(62) Divisional to Application No : NA<br />

Filed on : NA<br />

(71) Name <strong>of</strong> Applicant:<br />

ASAHI KASEI PHARMA CORPORATION.,<br />

Address <strong>of</strong> <strong>the</strong> Applicant:<br />

9-1, KANDA MITOSHIRO-CHO, CHIYODA-KU,<br />

TOKYO 101-8418, JAPAN.<br />

(72) Name <strong>of</strong> <strong>the</strong> Inventor:<br />

ICHIRO KOGUMA<br />

FUJIHARU NAGOYA<br />

Filed U/S 5(2) before The <strong>Patents</strong> (Amendment)<br />

Act, 2005: NO<br />

(57) Abstract:<br />

A hydrophilic microporous membrane comprising a <strong>the</strong>rmoplastic resin, having been subjected to hydrophilizing treatment and having a<br />

maximum pore size <strong>of</strong> 10 to 100nm, wherein when 3 wt% bovine immunoglobulin having a monomer ratio <strong>of</strong> 80 wt% or more is filtered<br />

at a constant pressure <strong>of</strong> 0.3 MPa, an average permeation rate (liter/m 2 /h) for 5 minutes from <strong>the</strong> start <strong>of</strong> filtration (briefly referred to as<br />

globulin permeation rate A) satisfies <strong>the</strong> following formula (1) and an average permeation rate (liter/m 2 /h) for 5 minutes from <strong>the</strong> time<br />

point <strong>of</strong> 55 minutes after <strong>the</strong> start <strong>of</strong> filtration (briefly referred to as globulin permeation rate B) satisfies <strong>the</strong> following formula (2):<br />

Globulin permeation rage A> 0.0015 x maximum pore size (nm) 2.75 (1) Globulin permeation rate B/globulin permeation rate A > 0.2 (2).<br />

(FIG). nil<br />

The Patent Office Journal 09/06/2006 11051

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