Patent US3984286A successfully refreshed from Google Patents.
US3984286A
Expired / Lapsed
US
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Apparatus and method for conducting fermentation
Assignee: Phillips Petroleum Co
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Filing: 1975-03-06
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Granted: 1976-10-05
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Expires: 1995-03-06
Abstract
Abstract An apparatus and method for microbial growth by fermentation with the apparatus including a plurality of vessels connected in series. The fermentation vessels include a prefermenter which feeds microorganism-containing effluent continuously to an intermediate fermenter in which the majority of fermentation is conducted. The intermediate fermenter feeds microorganism-containing effluent to a secondary fermenter in which portions of the feedstock are consumed substantially to extinction. Preferably heat exchangers for each of the vessels are connected in series and an oxygen-containing gas which is partially depleted of oxygen can be fed from the intermediate fermenter to the other fermenters in series.
Inventors
- 👤 Emil A. Malick
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 18:18
CPC Classifications
C; C12; C12M; C12M41/00; C12M41/12; C12M41/18; C12M41/24; C12M23/00; C12M23/58; C12M27/00; C12M27/18; C12M27/24; C12M29/00; C12M29/06; Y; Y10; Y10S; Y10S435/00; Y10S435/804; Y10S435/812; Y10S435/819
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
304 words
An apparatus for microbial growth by fermentation, said apparatus comprising: a. a prefermenter; b. an intermediate fermenter connected in series, by a first conduit, with and downstream of said prefermenter, whereby effluent from said prefermenter is fed to said intermediate fermenter, said intermediate fermenter having a volume substantially larger than said prefermenter; c. a draft tube mounted in said intermediate fermenter; d. an impeller positioned adjacent said draft tube and operable to effect flow of media through said draft tube; e. first heat exchange means in heat transfer relation with said intermediate fermenter and connected to a source of coolant; f. a secondary fermenter connected in series by a second conduit with and downstream of said intermediate fermenter whereby effluent from said intermediate fermenter is fed to said secondary fermenter; g. first means communicating with said intermediate fermenter and operable for introducing feedstock and oxygen into said intermediate fermenter; h. second heat exchange means in heat transfer relation with said secondary fermenter and is connected in series with and downstream of said first heat exchange means; i. third heat exchange means in heat transfer relation with said prefermenter and is connected in series with and downstream of said first heat exchange means; j. a second conduit connecting said intermediate fermenter with said secondary fermenter and forming a flow path therebetween for conducting oxygen from said intermediate fermenter to said secondary fermenter; k. a third conduit communicating between said intermediate fermenter and said prefermenter forming a flow path for conducting oxygen from said intemediate fermenter to said prefermenter; and l. a vessel communicating with said first conduit between said prefermenter and said intermediate fermenter wherein effluent from said prefermenter flows into said vessel before flowing into said intermediate fermenter with said vessel having mixing means operably associated therewith and also having inlet means opening thereinto.
Claim 2
Independent Claim
304 words
An apparatus for microbial growth by fermentation, said apparatus comprising: a. a prefermenter; b. an intermediate fermenter connected in series, by a first conduit, with and downstream of said prefermenter, whereby effluent from said prefermenter is fed to said intermediate fermenter, said intermediate fermenter having a volume substantially larger than said prefermenter; c. a draft tube mounted in said intermediate fermenter; d. an impeller positioned adjacent said draft tube and operable to effect flow of media through said draft tube; e. first heat exchange means in heat transfer relation with said intermediate fermenter and connected to a source of coolant; f. a secondary fermenter connected in series by a second conduit with and downstream of said intermediate fermenter whereby effluent from said intermediate fermenter is fed to said secondary fermenter; g. first means communicating with said intermediate fermenter and operable for introducing feedstock and oxygen into said intermediate fermenter; h. second heat exchange means in heat transfer relation with said secondary fermenter and is connected in series with and downstream of said first heat exchange means; i. third heat exchange means in heat transfer relation with said prefermenter and is connected in series with and downstream of said first heat exchange means; j. a second conduit connecting said intermediate fermenter with said secondary fermenter and forming a flow path therebetween for conducting oxygen from said intermediate fermenter to said secondary fermenter; k. a third conduit communicating between said intermediate fermenter and said prefermenter forming a flow path for conducting oxygen from said intemediate fermenter to said prefermenter; and l. a vessel communicating with said first conduit between said prefermenter and said intermediate fermenter wherein effluent from said prefermenter flows into said vessel before flowing into said intermediate fermenter with said vessel having mixing means operably associated therewith and also having inlet means opening thereinto.
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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) | 1979-10-05 | 1980-04-05 | 1980-10-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-10-05 | 1984-04-05 | 1984-10-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-10-05 | 1988-04-05 | 1988-10-05 | $7700.00 | Window Closed / Lapsed |