IP Library Granted Patent US 10,227,616
Granted Patent B2
US 10,227,616 · App. 15/303,931 · Granted Mar 12, 2019

Process for the production of 1,4-butanediol

Inventors: Maria Dani (Capua, IT); Giuseppe Ruggiero (San Nicola La Strada, IT); Davide Perini (Romentino, IT); Alice Bianchi (Assago, IT)
Assignees: Novamont S.P.A.; Genomatica, Inc.
C12P7/18
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Quick Facts
Patent No.
US 10,227,616
App. No.
15/303,931
Granted
Mar 12, 2019
Kind
B2
Abstract

Process for the synthesis of 1,4-butanediol comprising fermentation of a culture medium by a microorganism provided with at least one metabolic pathway for the synthesis of 1,4-butanediol and able to use saccharose, in which said culture medium comprises a glucose and saccharose mixture comprising, based on the combined weight of glucose and saccharose, 10-90% by weight of saccharose and 10-90% by weight of glucose.

Claims (26)

1. A process for the synthesis of 1,4-butanediol comprising fermentation of a culture medium by a microorganism belonging to the species Escherichia coli , provided with at least one metabolic pathway for the synthesis of 1,4-butanediol and able to use saccharose by means of at least one operon for the assimilation of saccharose, in which said culture medium comprises a glucose and saccharose mixture comprising, based on the combined weight of glucose and saccharose, 10-90% by weight of saccharose and 10-90% by weight of glucose, said operon being selected from the scr regulon from the Escherichia coli strain H155 or the regulon csc of the Escherichia coli strain W or both.

2. The process according to claim 1 , further comprising:

i. production of 1,4-butanediol; and

ii. purification of the 1,4-butanediol obtained in step i.

3. The process according to claim 2 , in which the concentration of said glucose and saccharose mixture in the culture medium is from 10 to 100 g/L.

4. The process according to claim 1 , wherein the culture medium comprises sugars different from saccharose and glucose amount up to 20 wt % with respect to the total amount of sugars in the culture medium.

5. The process according to claim 1 , in which during fermentation, the operating conditions are as follows: agitation rate=800−900 rpm, air flow 0.4−1 Pa*m 3 /s, pH 6-7, temperature 30-37° C.

6. The process according to claim 1 , in which said microorganism the metabolic pathway of synthesis of 1,4-butanediol has been created artificially.

7. The process according to claim 2 , in which said step ii comprises the following steps:

(ii-a) separation of a liquid phase containing 1,4-butanediol from one or more solid phases;

(ii-b) purification of the liquid phase containing 1,4-butanediol.

8. The process according to claim 7 , in which said step (ii-a) one or more treatments are carried out chosen from settling, centrifugation, filtration, microfiltration, nanofiltration, ultrafiltration, and osmosis.

9. The process according to claim 7 , in which in said step (ii-b) one or more treatments are carried out chosen from among evaporation, distillation, and crystallization.

10. Process according to claim 7 , in which said step (ii-b) comprises the steps of:

(ii-b-1) separate, by means of heating, at least one vapour phase and at least one condensate;

(ii-b-2) condense at least one part of said at least one vapour phase, obtaining a final composition essentially comprising 1,4-butanediol.

11. The process according to claim 1 , wherein the glucose and saccharose mixture comprises, based on the combined weight of glucose and saccharose, 20-80% by weight of saccharose and 20-80% by weight of glucose.

12. The process according to 2, wherein the culture medium comprises sugars different from saccharose and glucose amount up to 20 wt % with respect to the total amount of sugars in the culture medium.

13. The process according to claim 3 , wherein the culture medium comprises sugars different from saccharose and glucose amount up to 20 wt % with respect to the total amount of sugars in the culture medium.

14. The process according to claim 2 , in which during fermentation, the operating conditions are as follows: agitation rate=800-900 rpm, air flow 0.4-1 Pa*m 3 /s, pH 6-7, temperature 30-37° C.

15. The process according to claim 3 , in which during fermentation, the operating conditions are as follows: agitation rate=800-900 rpm, air flow 0.4-1 Pa*m 3 /s, pH 6-7, temperature 30-37° C.

16. The process according to claim 4 , in which during fermentation, the operating conditions are as follows: agitation rate=800-900 rpm, air flow 0.4-1 Pa*m 3 /s, pH 6-7, temperature 30-37° C.

17. The process according to claim 2 , in which said microorganism the metabolic pathway of synthesis of 1,4-butanediol has been created artificially.

18. The process according to claim 3 , in which said microorganism the metabolic pathway of synthesis of 1,4-butanediol has been created artificially.

19. The process according to claim 4 , in which said microorganism the metabolic pathway of synthesis of 1,4-butanediol has been created artificially.

20. The process according to claim 5 , in which said microorganism the metabolic pathway of synthesis of 1,4-butanediol has been created artificially.

Assignments (4)
SECURITY INTEREST Recorded Feb 10, 2026
From: GENOMATICA, INC.
To: AGAIN BIO APS
Reel/Frame 074708/0001 →
SECURITY INTEREST Recorded Dec 9, 2025
From: GENOMATICA, INC.
To: NOVO HOLDINGS A/S, AS COLLATERAL AGENT
Reel/Frame 073915/0027 →
SECURITY INTEREST Recorded Jun 2, 2025
From: GENOMATICA, INC.
To: OXFORD FINANCE LLC
Reel/Frame 071471/0770 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 13, 2016
From: DANI, MARIA; RUGGIERO, GUISEPPE; PERINI, DAVIDE; BIANCHI, ALICE
To: NOVAMONT S.P.A.; GENOMATICA, INC.
Reel/Frame 040007/0982 →
Priority Claims (1)
IT MI2014A0710 · Apr 16, 2014 · national
Continuity (1)
Related Publication 20170029852A1 · Feb 2, 2017