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US4649114A Expired / Lapsed US ⏱️ 0.0 years remaining

Oxygen permeable membrane in fermenter for oxygen enrichment of broth

Assignee: B Braun Surgical AG
•
Filing: 1982-12-03
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Granted: 1987-03-10
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Expires: 2002-12-03
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Abstract

Abstract The growth of animal cells in a fermenter is promoted by enriching the liquid nutrient medium or broth with oxygen diffused into the liquid through a permeable membrane, such as one made of silicone rubber or polytetrafluoroethylene (Teflon). Superior cell growth in larger volumes is achieved by feeding in the oxygen in this way instead of bubbling it in.

Inventors

  • 👤 Herbert G. Miltenburger
  • 👤 Sigfried Hessberg

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 19:15
CPC Classifications
C; C12; C12M; C12M29/00; C12M29/04; C12M23/00; C12M23/24

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 149 words
In a fermentation vessel for propagating animal cells in suspension cultures and monolayer cultures in which oxygen must be supplied to the cells in a liquid nutrient medium in the vessel for cell metabolism and multiplication, the improvement comprising a permeable membrane partially defining a chamber or volume in the fermentation vessel and made of a polymeric material on which the cells do not grow to a significant extent but through which oxygen can diffuse directly, without bubbling, into at least a 4 liter volume of the liquid nutrient medium containing the cells; the membrane being of a size and shape so that a sufficient amount of oxygen is diffused into the liquid so as to enable cell propagation; conduit means communicating with the chamber from outside the vessel for supplying oxygen to the chamber for diffusion through the membrane; and mechanical liquid-agitation means located within the fermentation vessel.
Claim 2
Dependent Claim 149 words
In a fermentation vessel for propagating animal cells in suspension cultures and monolayer cultures in which oxygen must be supplied to the cells in a liquid nutrient medium in the vessel for cell metabolism and multiplication, the improvement comprising a permeable membrane partially defining a chamber or volume in the fermentation vessel and made of a polymeric material on which the cells do not grow to a significant extent but through which oxygen can diffuse directly, without bubbling, into at least a 4 liter volume of the liquid nutrient medium containing the cells; the membrane being of a size and shape so that a sufficient amount of oxygen is diffused into the liquid so as to enable cell propagation; conduit means communicating with the chamber from outside the vessel for supplying oxygen to the chamber for diffusion through the membrane; and mechanical liquid-agitation means located within the fermentation vessel.
Claim 3
Dependent Claim 18 words
An improved fermentation vessel according to claim 1 in which the polymeric material is silicone rubber or polytetrafluoroethylene.
Claim 4
Dependent Claim 15 words
An improved fermentation vessel according to claim 1 in which the membrane is a tube.
Claim 5
Dependent Claim 20 words
An improved fermentation vessel according to claim 3 in which the tube wall is about 0.6 to 1.2 mm thick.
Claim 6
Dependent Claim 17 words
An improved fermentation vessel according to claim 3 in which the tube is on a rigid support.
Claim 7
Dependent Claim 17 words
An improved fermentation vessel according to claim 5 in which the rigid support is a heat exchanger.
Claim 8
Independent Claim 112 words
A method comprising growing animal cells in suspension cultures and monolayer cultures in a fermentation vessel containing at least a 4 liter volume of a liquid nutrient medium, and supplying the cells with oxygen through a permeable membrane partially defining a chamber or volume in the fermentation vessel and made of a polymeric material on which almost no cell growth takes place, so that the oxygen diffuses directly without bubbling into the liquid medium; the oxygen being supplied to the chamber from outside the vessel; and the membrane being of a size and shape so that a sufficient amount of oxygen is diffused into the liquid so as to enable cell propagation.
Claim 9
Independent Claim 112 words
A method comprising growing animal cells in suspension cultures and monolayer cultures in a fermentation vessel containing at least a 4 liter volume of a liquid nutrient medium, and supplying the cells with oxygen through a permeable membrane partially defining a chamber or volume in the fermentation vessel and made of a polymeric material on which almost no cell growth takes place, so that the oxygen diffuses directly without bubbling into the liquid medium; the oxygen being supplied to the chamber from outside the vessel; and the membrane being of a size and shape so that a sufficient amount of oxygen is diffused into the liquid so as to enable cell propagation.
Claim 10
Dependent Claim 17 words
A method according to claim 7 in which the membrane is in the form of a tube.
Claim 11
Dependent Claim 20 words
A method according to claim 8 in which the tube has a wall thickness of about 0.6 to 1.2 mm.
Claim 12
Dependent Claim 13 words
A method according to claim 8 in which the tube is silicone rubber.
Claim 13
Dependent Claim 19 words
A method according to claim 7 in which the membrane is a tube spirally wound on a rigid support.
Claim 14
Dependent Claim 15 words
A method according to claim 11 in which the rigid support is a heat exchanger.
Claim 15
Dependent Claim 15 words
A method according to claim 7 in which the animal cells are from a non-vertebrate.
Claim 16
Dependent Claim 14 words
A method according to claim 13 in which the animal cells are insect cells.
Claim 17
Dependent Claim 31 words
A method according to claim 7 in which cell growth continues until cell multiplication increases the cell population to at least 20 times the cell population at the start of fermentation.
Claim 18
Dependent Claim 16 words
A method according to claim 7 in which the polymeric material is silicone rubber or polytetrafluoroethylene.

References Cited (Backward Citations)

US2522947A Cited
US3927981A Cited
US3850748A Cited
US3997396A Cited
GB1530705A Cited
US4259449A Cited
US4242460A Cited
US4391912A Cited
US4416993A Cited
US4537860A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-03-09 1990-09-08 1991-03-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-03-09 1994-09-08 1995-03-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-03-09 1998-09-08 1999-03-10 $7700.00 Window Closed / Lapsed

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