US4442206A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of using isotropic, porous-wall polymeric membrane, hollow-fibers for culture of microbes
Assignee: Leland Stanford Junior University
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Filing: 1983-05-04
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Granted: 1984-04-10
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Expires: 2003-05-04
Abstract
Abstract Hollow fiber reactors for growing microbial cells. Isotropic hollow fibers are supported in a housing inoculated with cells. Nutrient medium passing through the lumen undergoes a pressure drop resulting in radial convective flow: the nutrient medium flows outwardly from the lumen into the surrounding area adjacent the entry port and fluid surrounding the hollow fiber flows into the lumen adjacent the exit port. With the efficient distribution of nutrients and removal of product, high cell densities are achieved providing for high product yields per unit reactor volume.
Inventors
- 👤 Alan S. Michaels
- 👤 Channing R. Robertson
- 👤 Stanley N. Cohen
- 👤 Douglas S. Inloes
- 👤 William J. Smith
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 23:41
CPC Classifications
B; B01; B01D; B01D63/00; B01D63/02; B01D69/00; B01D69/14; B01D69/141; C; C12; C12M; C12M29/00; C12M29/10; C12M29/16; Y; Y10; Y10S; Y10S435/00; Y10S435/813
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
273 words
A method for the efficient cultivation of microbial cells employing a microbiological reactor comprising isotropic, porous-wall polymeric hollow-fibers having a cell free zone and a cell containing zone, said cell containing zone substantially located in the space surrounding said hollow-fiber and partially extending beneath the outer surface of said hollow-fibers, wherein both zones are perfused with nutrient medium and separated by a porous barrier permeable to said nutrient medium and impermeable to said cells, said method comprising: continuously introducing at an entry port of said cell free zone at a pressure greater than the pressure of said nutrient medium in said cell containing zone a nutrient medium stream, whereby said nutrient medium flows out of said cell free zone into said cell containing zone and said microbial cells metabolize nutrients in said nutrient medium to products to produce a product-containing spent nutrient medium in said cell containing zone and said cells further proliferating within said cell containing zone to a cell density greater than 10 12 cell/ml; continuously flowing said nutrient medium stream remaining in said cell free zone toward an exit port in said cell free zone while reducing the pressure of said nutrient medium stream, so that the pressure of said nutrient medium stream at said exit port is below the pressure of said product-containing nutrient medium in said cell containing zone, whereby product-containing spent nutrient medium in said cell containing zone flows into said cell free zone near said exit port and mixes with said nutrient medium in said cell free zone to form a mixture; and continuously removing said mixture from said exit port of said cell free zone.
Claim 2
Independent Claim
273 words
A method for the efficient cultivation of microbial cells employing a microbiological reactor comprising isotropic, porous-wall polymeric hollow-fibers having a cell free zone and a cell containing zone, said cell containing zone substantially located in the space surrounding said hollow-fiber and partially extending beneath the outer surface of said hollow-fibers, wherein both zones are perfused with nutrient medium and separated by a porous barrier permeable to said nutrient medium and impermeable to said cells, said method comprising: continuously introducing at an entry port of said cell free zone at a pressure greater than the pressure of said nutrient medium in said cell containing zone a nutrient medium stream, whereby said nutrient medium flows out of said cell free zone into said cell containing zone and said microbial cells metabolize nutrients in said nutrient medium to products to produce a product-containing spent nutrient medium in said cell containing zone and said cells further proliferating within said cell containing zone to a cell density greater than 10 12 cell/ml; continuously flowing said nutrient medium stream remaining in said cell free zone toward an exit port in said cell free zone while reducing the pressure of said nutrient medium stream, so that the pressure of said nutrient medium stream at said exit port is below the pressure of said product-containing nutrient medium in said cell containing zone, whereby product-containing spent nutrient medium in said cell containing zone flows into said cell free zone near said exit port and mixes with said nutrient medium in said cell free zone to form a mixture; and continuously removing said mixture from said exit port of said cell free zone.
Claim 3
Dependent Claim
42 words
A method according to claim 1, wherein said porous barrier has a porosity of less than about 50% and pores of a size having as their largest dimension a size less than about 50% of the smallest dimension of said microbial cells.
Claim 4
Dependent Claim
25 words
A method according to claim 2, wherein said cell free zone is a plurality of hollow fibers of less than about 1 mm outer diameter.
Claim 5
Dependent Claim
12 words
A method according to claim 1, wherein said microbial cells are prokaryotes.
Claim 6
Dependent Claim
12 words
A method according to claim 1, wherein said microbial cells are yeast.
Claim 7
Dependent Claim
12 words
A method according to claim 1, wherein said microbial cells are fungi.
Claim 8
Independent Claim
16 words
A method according to any of claims 1, or 4, wherein said product includes a polypeptide.
Claim 9
Dependent Claim
12 words
A method according to claim 7, wherein said polypeptide is a protein.
Claim 10
Dependent Claim
12 words
A method according to claim 8, wherein said protein is an enzyme.
Claim 11
Dependent Claim
13 words
A method according to claim 1, wherein said product includes a non-proteinaceous product.
Claim 12
Dependent Claim
12 words
A method according to claim 10, wherein said non-proteinaceous product is ethanol.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-04-10 | 1987-10-10 | 1988-04-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-04-10 | 1991-10-10 | 1992-04-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-04-10 | 1995-10-10 | 1996-04-10 | $7700.00 | Window Closed / Lapsed |