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US 11,142,783 B2Granted
Seed train for large scale enzyme production
AssigneeDsm IP Assets B.V.
InventorsAndre De Castro Bizarro Duarte Canelas, Wouter Adrianus Van Winden
Life of this patent
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Abstract
The invention relates to an optimized seed train expansion process.
Claims18
A process for producing an enzyme or an enzyme composition, the process comprising:
- a) preparing a fungal inoculum comprising fungal cells in an inoculum bioreactor,
- b) transferring the inoculum to a first of two or more production bioreactors, said first production bioreactor being ready for inoculation,
- c) culturing the fungal cells in the first production bioreactor to produce the enzyme or enzyme composition,
- d) emptying a second of the two or more production bioreactors, said second production bioreactor having reached the end of fermentation, and preparing the second production bioreactor for a new production fermentation,
- e) after (b), but before completion of (d), preparing a second fungal inoculum comprising fungal cells in the inoculum bioreactor,
- f) transferring the second inoculum to the second of the two or more production bioreactors, said second production bioreactor being ready for inoculation,
- g) culturing the fungal cells in the second production bioreactor to produce the enzyme or enzyme composition,
- h) emptying the first of the two or more production bioreactors, said first production bioreactor having reached the end of fermentation, and preparing the first production bioreactor for a new production fermentation, and
- i) after (f), but before completion of (h), repeating at least (a), and after completion of (h) repeating at least (b)-(e),
- wherein the first and/or second production bioreactors have a gross vessel volume of 20,000 l to 300,000 l, the inoculum bioreactor has a gross vessel volume of 300 l to 15,000 l and the ratio of the gross vessel volume of the inoculum bioreactor to the gross vessel volume of the first production bioreactor is from 2% to 4.5%, and/or the ratio of the gross vessel volume of the inoculum bioreactor to the gross vessel volume of the second production bioreactor is from 2% to 4.5%.
7 more elements
A process for producing an enzyme or an enzyme composition, the process comprising:
- a) preparing a fungal inoculum comprising fungal cells in an inoculum bioreactor,
- b) transferring the inoculum to a first of three or more production bioreactors, said first production bioreactor being ready for inoculation,
- c) culturing the fungal cells in the first production bioreactor to produce the enzyme or enzyme composition,
- d) emptying a second of the three or more production bioreactors, said second production bioreactor having reached the end of fermentation, and preparing the second production bioreactor for a new production fermentation,
- e) after (b), but before completion of (d), preparing a second fungal inoculum comprising fungal cells in the inoculum bioreactor,
- f) transferring the second inoculum to the second of the three or more production bioreactors, said second production bioreactor being ready for inoculation,
- g) culturing the fungal cells in the second production bioreactor to produce the enzyme or enzyme composition,
- h) emptying a third of the three or more production bioreactors, said third production bioreactor having reached the end of fermentation, and preparing the third production bioreactor for a new production fermentation,
- i) after (f), but before completion of (h), preparing a third fungal inoculum comprising fungal cells in the inoculum bioreactor,
- j) transferring the third inoculum to the third of the three or more production bioreactors, said third production bioreactor being ready for inoculation,
- k) culturing the fungal cells in the third production bioreactor to produce the enzyme or enzyme composition,
- l) emptying the first of the three or more production bioreactors, said first production bioreactor having reached the end of fermentation, and preparing the first production bioreactor for a new production fermentation, and
- m) after (j), but before completion of (l), repeating at least (a), and after completion of (h) repeating at least (b)-(e),
- wherein the first, second and/or third production bioreactor have a gross vessel volume of 20,000 l to 300,000 l, the inoculum bioreactor has a gross vessel volume of 300 l to 15,000 l and the ratio of the gross vessel volume of the inoculum bioreactor to the gross vessel volume of the first production bioreactor is from 2% to 4.5%, and/or the ratio of the gross vessel volume of the inoculum bioreactor to the gross vessel volume of the second production bioreactor is from 2% to 4.5%, and/or the ratio of the gross vessel volume of the inoculum bioreactor to the gross vessel volume of the third production bioreactor is from 2% to 4.5%.
11 more elements
Dependencies are inferred from the claim text.