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Process for sterilizing a filtration device

Assignee: Asahi Kasei Corp
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Filing: 1986-04-11
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Granted: 1989-06-20
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Expires: 2006-04-11
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Abstract

Abstract A process for sterilizing a filtration device which comprises employing therein a hollow fiber type module having hollow fibers of heat resistant polymer with a heat distortion temperature of 70° C. or higher under a load of 18.6 kg/cm 2 and with a pore diameter of less than 0.45 μm and having a difference in average linear expansion coefficient between the sealing material for fixing the end portions of the hollow fibers in the module case, at a temperature of 20°-121° C. of 7×10 -5 /° C. or lower, and passing steam from the raw water side of the module to the filtrate side thereof, while withdrawing all or a part of the raw water and filtrate which partially fill the module or alternatively after withdrawal of raw water and filtrate.

Inventors

  • 👤 Tatuo Nejigaki
  • 👤 Yoshimi Kakutani

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 01:10
CPC Classifications
A; A61; A61M; A61M1/00; A61M1/14; A61M1/16; A61M1/168; A61M1/1686; A61M1/36; A61M1/3621; A61M1/3643; A61M1/3644; A61M1/365; B; B01; B01D; B01D63/00; B01D63/02; B01D63/021; B01D63/022; B01D63/023; B01D65/00; B01D65/02; B01D65/022; B01D2321/00; B01D2321/08

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 227 words
A process for sterilizing a filtration device containing residual raw water and filtrate and having a raw water side and a filtrate side and which employs therein a hollow, fiber type filtration module comprising hollow fibers disposed in a module case, said hollow fibers having end portions which are fixed in said module case by a sealing material, said hollow fibers being made of a heat resistant polymer with a heat distortion temperature of 70° C. or higher under a load of 18.6 kg/cm 2 and containing a pore diameter of less than 0.45 μm and the sealing material having a diference in the average linear expansion coefficient between it and the material of the module case of 7×10 -5 /°C. or lower, at a temperature of 20°-121° C., which comprises (i) discontinuing filtration, (ii) passing sterilizing steam from the raw water side of the module to the filtrate side thereof, after pushing out the raw water from the raw water inlet of the module and filtrate from the module, with said sterilizing steam and (iii) preventing the filtrate side of the filtration device from developing a negative pressure by introducing a fluid selected from the group consisting of water and a sterilized gas into the filtration device from a raw water side during the natural cooling which takes place after the steam sterilization has been completed.
Claim 2
Dependent Claim 227 words
A process for sterilizing a filtration device containing residual raw water and filtrate and having a raw water side and a filtrate side and which employs therein a hollow, fiber type filtration module comprising hollow fibers disposed in a module case, said hollow fibers having end portions which are fixed in said module case by a sealing material, said hollow fibers being made of a heat resistant polymer with a heat distortion temperature of 70° C. or higher under a load of 18.6 kg/cm 2 and containing a pore diameter of less than 0.45 μm and the sealing material having a diference in the average linear expansion coefficient between it and the material of the module case of 7×10 -5 /°C. or lower, at a temperature of 20°-121° C., which comprises (i) discontinuing filtration, (ii) passing sterilizing steam from the raw water side of the module to the filtrate side thereof, after pushing out the raw water from the raw water inlet of the module and filtrate from the module, with said sterilizing steam and (iii) preventing the filtrate side of the filtration device from developing a negative pressure by introducing a fluid selected from the group consisting of water and a sterilized gas into the filtration device from a raw water side during the natural cooling which takes place after the steam sterilization has been completed.
Claim 3
Dependent Claim 36 words
The process of claim 1 wherein the hollow, fiber type filtration module is a fiber membrane made of a material selected from the group consisting of polyvinlylidene fluoride, polypropylene, polyphenylene oxide, ethylene-tetrafluoro-ethylene copolymer, polysulfone, and polyethersulfone.
Claim 4
Dependent Claim 28 words
The process of claim 1 wherein the sterilizing steam has a temperature of 121° to 125° C. and a pressure of from 1 to 1.5 kg/cm 2 .
Claim 5
Dependent Claim 38 words
The process of claim 1 wherein a sterilizing gas having a pressure of 0.5 to 1 kg/cm 2 is introduced and said sterilizing gas is a member selected from the group consisting of air, nitrogen, oxygen, and helium.
Claim 6
Dependent Claim 20 words
The method of claim 1 wherein the sealing material is an epoxy resin or an epoxy resin containing silica powder.

References Cited (Backward Citations)

DE2524079A1 Cited
DE2446991A1 Cited
US4176156A Cited
US4366051A Cited
US4268279A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-06-19 1992-12-19 1993-06-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-06-19 1996-12-19 1997-06-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-06-19 2000-12-19 2001-06-20 $7700.00 Window Closed / Lapsed

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