IP Library Granted Patent US 8,324,442
Granted Patent B2
US 8,324,442 · App. 12/659,216 · Granted Dec 4, 2012

Microbial derived isoprene and methods for making the same

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,324,442
App. No.
12/659,216
Granted
Dec 4, 2012
Kind
B2
Abstract

A method for producing isoprene comprising an aqueous medium including genetically modified host cells capable of producing isoprene, where the resulting isoprene composition is processed through at least one separation and/or purification process to provide an isoprene enriched composition and a system for doing the same.

Claims (48)

1. A method of purifying isoprene comprising:

a. obtaining a first gaseous composition comprising isoprene and water, wherein the gaseous composition comprises 1 part per million or less of C 2 -C 5 alkyne;

b. flowing the first gaseous composition through a first chiller wherein the first chiller has a temperature of between about 10° C. and about −15° C. thereby resulting in a second gaseous composition and wherein the second gaseous composition comprises less water than the first gaseous composition;

c. flowing the second gaseous composition through a second chiller wherein the second chiller has a temperature below −35° C.; and

d. collecting the resulting liquid isoprene composition.

2. The method of claim 1 , wherein the water is present in the first gaseous composition in an amount that is greater than 70% of its saturation amount.

3. The method of claim 1 , wherein the first gaseous isoprene composition further comprises carbon dioxide in an amount between about 0.1% and about 35% by volume.

4. The method of claim 1 , wherein the first gaseous composition further comprises 1 part per million or less of cyclopentadiene, piperylene and 1,4-pentadiene.

5. The method of claim 1 , wherein the first chiller is cooled using a propylene refrigeration system.

6. The method of claim 1 , wherein the first chiller is cooled using an ammonium refrigeration system.

7. The method of claim 1 , wherein the first gaseous composition is flowed through a drier prior to flowing through the first chiller.

8. The method of claim 1 , wherein the first gaseous composition is flowed through a drier after flowing through the first chiller.

9. The method of claim 1 , wherein the second chiller has a temperature of about −60° C. to about −85° C.

10. The method of claim 1 , wherein the second chiller has a temperature of less than about −65° C.

11. The method of claim 1 , wherein the second chiller is cooled using an ethylene refrigeration system.

12. The method of claim 1 , further comprising nitrogen stripping the liquid isoprene composition.

13. The method of claim 1 , further comprising passing the first gaseous composition through a modified zeolite membrane to separate hydrocarbon impurities from the isoprene.

14. The method of claim 1 , further comprising passing the second gaseous composition through a modified zeolite membrane to separate hydrocarbon impurities from the isoprene.

15. The method of claim 1 , further comprising passing the liquid isoprene composition through a modified zeolite membrane to separate hydrocarbon impurities from the isoprene.

16. A method of purifying isoprene comprising:

a. obtaining a first gaseous composition comprising:

i) isoprene in an amount between about 0.1% and about 15% by volume;

ii) carbon dioxide in an amount between about 0.04% and about 35% by volume;

iii) oxygen in an amount between about 1% and about 20% by volume;

iv) nitrogen in an amount greater than about 50% by volume;

v) argon in an amount less than about 0.9% by volume;

vi) water in an amount greater than about 70% of its saturation amount;

vii) 1 part per million or less of C 2 -C 5 alkyne, cyclopentadiene, piperylene, and 1,4-pentadiene; and

viii) ethanol;

b. flowing the first gaseous composition through a first chiller and an operably connected flash drum, wherein the first chiller has a temperature of between about 10° C. and about −15° C. thereby resulting in a second gaseous composition and wherein the second gaseous composition comprises less water than the first gaseous composition;

c. flowing the second gaseous composition through a second chiller and an operably connected flash drum, wherein the second chiller has a temperature between about −35° C. and about −85° C.; and

d. collecting the resulting liquid isoprene composition.

17. The method of claim 16 , wherein the first gaseous composition is obtained by culturing a plurality of host cells capable of making isoprene.

18. The method of claim 17 , wherein the host cells are yeast.

19. The method of claim 17 , wherein the host cells are Saccharomyces cerevisie .

20. The method of claim 16 , wherein the resulting second gaseous composition comprises less than about 3% by weight of water.

21. The method of claim 16 , wherein the resulting liquid isoprene composition comprises less than about 1% by weight of water.

22. The method of claim 16 , wherein the resulting liquid isoprene composition comprises less than about 1% by weight of carbon dioxide.

23. The method of claim 16 , wherein the resulting liquid isoprene composition comprises less than about 1% by weight of nitrogen.

24. The method of claim 16 , wherein the resulting liquid isoprene composition comprises:

i) at least 65% isoprene by weight; and

ii) less than 1% water by weight.

25. The method of claim 16 , wherein the resulting liquid isoprene composition comprises less than about 1% by weight of ethanol.

26. The method of claim 16 , further comprising nitrogen stripping the liquid isoprene composition.

27. The method of claim 26 , wherein the liquid isoprene composition comprises at least 70% isoprene by weight and less than 1% by weight of dissolved carbon dioxide.

28. The method of claim 26 , wherein the liquid isoprene composition comprises at least 90% isoprene by weight and less than 1% by weight of dissolved carbon dioxide.

29. The method of claim 26 , wherein the liquid isoprene composition comprises at least 95% isoprene by weight and less than 1% by weight of dissolved carbon dioxide.

30. The method of claim 26 , wherein the liquid isoprene composition comprises at least 99% isoprene by weight and less than 0.05% by weight of dissolved carbon dioxide.

Assignments (20)
SECURITY INTEREST Recorded May 24, 2024
From: AMYRIS, INC.
To: EUAGORE, LLC
Reel/Frame 067528/0467 →
SECURITY INTEREST Recorded Aug 17, 2023
From: AMYRIS, INC.; AMYRIS CLEAN BEAUTY, INC.; AMYRIS FUELS, LLC; AB TECHNOLOGIES LLC; APRINNOVA, LLC; AMYRIS-OLINKA, LLC; ONDA BEAUTY INC.; UPLAND 1 LLC; AMYRIS ECO-FAB LLC; CLEAN BEAUTY 4U HOLDINGS, LLC; AMYRIS CLEAN BEAUTY LATAM LTDA; INTERFACES INDUSTRIA E COMERCIA DE COSMETICOS LTDA; AMYRIS BIOTECHNOLOGIA DO BRASIL LTDA; AMYRIS EUROPE TRADING B.V. (NETHERLANDS); AMYRIS BIO PRODCUTS PORTUGAL, UNIPESSOAL, LDA; BEAUTY LABS INTERNATIONAL LIMITED; AMYRIS UK TRADING LIMITED
To: EUAGORE, LLC
Reel/Frame 064619/0778 →
SECURITY INTEREST Recorded Aug 3, 2023
From: AMYRIS CLEAN BEAUTY, INC.; AMYRIS FUELS, LLC; AB TECHNOLOGIES LLC; AMYRIS, INC.
To: MUIRISC, LLC
Reel/Frame 064492/0518 →
RELEASE OF SECURITY INTEREST Recorded Feb 14, 2023
From: NAXYRIS S.A.
To: AMYRIS, INC.
Reel/Frame 062760/0753 →
RELEASE OF SECURITY INTEREST Recorded Feb 14, 2023
From: SCHOTTENFELD OPPORTUNITIES FUND II, L.P.
To: AMYRIS, INC.
Reel/Frame 062760/0818 →
SECURITY INTEREST Recorded Oct 18, 2022
From: AMYRIS, INC.
To: FORIS VENTURES, LLC
Reel/Frame 061703/0499 →
GRANT OF PATENT SECURITY INTEREST Recorded Nov 20, 2019
From: AMYRIS, INC.
To: SCHOTTENFELD OPPORTUNITIES FUND II, L.P.
Reel/Frame 051072/0310 →
RELEASE OF SECURITY INTEREST Recorded Aug 28, 2019
From: STEGODON CORPORATION
To: AMYRIS, INC.
Reel/Frame 050206/0606 →
SECURITY INTEREST Recorded Aug 16, 2019
From: AMYRIS, INC.
To: NAXYRIS S.A.
Reel/Frame 050081/0106 →
SECURITY INTEREST Recorded Jun 16, 2016
From: HERCULES CAPITAL INC.
To: STEGODON CORPORATION
Reel/Frame 039048/0251 →
SECURITY INTEREST Recorded Jun 3, 2016
From: AMYRIS, INC.
To: HERCULES TECHNOLOGY GROWTH CAPITAL, INC.
Reel/Frame 038878/0381 →
RELEASE OF SECURITY INTEREST Recorded Mar 31, 2014
From: MAXWELL (MAURITIUS) PTE LTD
To: AMYRIS, INC.
Reel/Frame 032578/0357 →
RELEASE OF SECURITY INTEREST Recorded Mar 28, 2014
From: TOTAL ENERGIES NOUVELLES ACTIVITES USA, SAS (F/K/A TOTAL GAS & POWER USA, SAS)
To: AMYRIS, INC.
Reel/Frame 032554/0001 →
RELEASE OF SECURITY INTEREST Recorded Mar 27, 2014
From: TOTAL ENERGIES NOUVELLES ACTIVITIES USA, SAS (F/K/A TOTAL GAS & POWER USA, SAS)
To: AMYRIS, INC.
Reel/Frame 032551/0828 →
SECURITY AGREEMENT Recorded Nov 8, 2013
From: AMYRIS, INC.
To: TOTAL ENERGIES NOUVELLES ACTIVITES USA
Reel/Frame 031607/0314 →
SECURITY AGREEMENT Recorded Oct 23, 2013
From: AMYRIS, INC.
To: MAXWELL (MAURITIUS) PTE LTD
Reel/Frame 031478/0933 →
CHANGE OF NAME Recorded Jun 7, 2013
From: AMYRIS BIOTECHNOLOGIES, INC.
To: AMYRIS, INC.
Reel/Frame 030575/0611 →
SECURITY AGREEMENT Recorded May 8, 2013
From: AMYRIS, INC.
To: TOTAL GAS & POWER USA, SAS
Reel/Frame 030378/0447 →
CHANGE OF NAME Recorded Sep 13, 2011
From: AMYRIS BIOTECHNOLOGIES, INC.
To: AMYRIS, INC.
Reel/Frame 026897/0682 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 10, 2010
From: MCPHEE, DEREK
To: AMYRIS BIOTECHNOLOGIES, INC.
Reel/Frame 024383/0662 →