IP Library Granted Patent US 10,144,683
Granted Patent B2
US 10,144,683 · App. 14/867,179 · Granted Dec 4, 2018

Method for collecting isoprene contained in fermented gas, and method for producing purified isoprene

Inventors: Hiroaki Rachi (Kanagawa, JP); Hiromoto Watanabe (Kanagawa, JP); Yosuke Nishio (Kanagawa, JP); Keiji Takita (Kanagawa, JP); Satoshi Hioki (Kanagawa, JP)
Assignee: Ajinomoto Co., Inc.
C07C7/12B01D53/047C07C7/005C07C7/13C12P5/007B01D2253/106B01D2257/7022B01D2259/402Y02E50/343
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Quick Facts
Patent No.
US 10,144,683
App. No.
14/867,179
Granted
Dec 4, 2018
Kind
B2
Abstract

Methods include contacting a fermented gas including isoprene with a porous adsorbent and desorbing isoprene adsorbed on the porous adsorbent. The fermented gas may be obtained by culturing a microorganism having an ability to produce isoprene.

Claims (48)

1. A method, comprising:

contacting a fermented gas comprising isoprene with a porous adsorbent; and

desorbing isoprene adsorbed on the porous adsorbent at a temperature of 80° C. or less;

wherein:

the fermented gas is obtained by culturing a microorganism having an ability to produce isoprene;

desorbing isoprene comprises desorbing isoprene gas; and

the porous adsorbent is a hydrophobidized silica gel with an average pore size of 60 Angstroms or less.

2. The method according to claim 1 , comprising recovering liquid isoprene by cooling the desorbed isoprene.

3. The method according to claim 1 , wherein the microorganism having an ability to produce isoprene is a bacterium of the genus Pantoea.

4. The method according to claim 1 , wherein desorbing isoprene adsorbed on the porous adsorbent comprises desorbing at a temperature of 60° C. or less.

5. The method according to claim 1 , comprising performing a pressure swing adsorption method.

6. The method according to claim 5 , wherein:

contacting the fermented gas with the porous adsorbent comprises contacting at a pressure (PI-1);

desorbing isoprene adsorbed on the porous adsorbent comprises desorbing at a pressure (PI-2); and

the pressures PI-1 and PI-2 satisfy PI-1-PI-2>50 kPa.

7. The method according to claim 5 , comprising, in sequence:

contacting the fermented gas with the porous adsorbent;

desorbing isoprene adsorbed on the porous adsorbent;

again contacting the fermented gas with the porous adsorbent; and

again desorbing isoprene adsorbed on the porous adsorbent.

8. The method according to claim 1 , comprising dehydrating the fermented gas before contacting the fermented gas with the porous adsorbent.

9. The method according to claim 1 , comprising removing an organic substance from the fermented gas before contacting the fermented gas with the porous adsorbent.

10. The method according to claim 1 , further comprising, after contacting the fermented gas with the porous adsorbent, discharging fermented gas having an isoprene concentration of 0.8 C0 or less;

wherein C0 is an isoprene concentration of the fermented gas contacted with the porous adsorbent.

11. A method, comprising:

culturing a microorganism having an ability to produce isoprene to obtain a fermented gas comprising isoprene;

contacting the fermented gas comprising isoprene with a porous adsorbent; and

desorbing isoprene adsorbed on the porous adsorbent at a temperature of 80° C. or less;

wherein:

desorbing isoprene comprises desorbing isoprene gas, and

the porous adsorbent is a hydrophobidized silica gel with an average pore size of 60 Angstroms or less.

12. The method according to claim 11 , comprising recovering liquid isoprene by cooling the desorbed isoprene.

13. The method according to claim 11 , wherein the microorganism having an ability to produce isoprene is a bacterium of the genus Pantoea.

14. The method according to claim 11 , wherein desorbing isoprene adsorbed on the porous adsorbent comprises desorbing at a temperature of 60° C. or less.

15. The method according to claim 11 , comprising performing a pressure swing adsorption method.

16. The method according to claim 15 , wherein:

contacting the fermented gas with the porous adsorbent comprises contacting at a pressure (PI-1);

desorbing isoprene adsorbed on the porous adsorbent comprises desorbing at a pressure (PI-2); and

the pressures PI-1 and PI-2 satisfy PI-1-PI-2>50 kPa.

17. The method according to claim 15 , comprising, in sequence:

contacting the fermented gas with the porous adsorbent;

desorbing isoprene adsorbed on the porous adsorbent;

again contacting the fermented gas with the porous adsorbent; and

again desorbing isoprene adsorbed on the porous adsorbent.

18. The method according to claim 11 , comprising dehydrating the fermented gas before contacting the fermented gas with the porous adsorbent.

19. The method according to claim 11 , comprising removing an organic substance from the fermented gas before contacting the fermented gas with the porous adsorbent.

20. The method according to claim 11 , further comprising, after contacting the fermented gas with the porous adsorbent, discharging fermented gas having an isoprene concentration of 0.8 C0 or less;

wherein C0 is an isoprene concentration of the fermented gas contacted with the porous adsorbent.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 20, 2016
From: RACHI, HIROAKI; WATANABE, HIROMOTO; NISHIO, YOSUKE; TAKITA, KEIJI; HIOKI, SATOSHI
To: AJINOMOTO CO., INC.
Reel/Frame 037528/0327 →
Priority Claims (1)
JP 2013-074262 · Mar 29, 2013 · national
Continuity (2)
Continuation PCTJP2014057869 · Mar 20, 2014
Related Publication 20160016867A1 · Jan 21, 2016