IP Library Granted Patent US 10,995,048
Granted Patent B2
US 10,995,048 · App. 16/682,059 · Granted May 4, 2021

Natural 1,2-alkanediols, compositions having natural 1,2-alkanediols and processes for making the same

Inventors: Rocco V. Burgo (Mullica Hill, NJ); Michael E. Wright (Hurricane, UT); Gary B. Mosser (Tabernacle, NJ); Michael J. Fevola (Belle Mead, NJ)
Assignee: INOLEX INVESTMENT CORPORATION
C07C29/04B01J21/04B01J23/06B01J37/08C07C1/24C07C11/02C07C11/107C07C29/48C07C29/80C07C31/20C11D3/2044A01N31/02A61K8/345A61L2/18A61Q5/00A61Q11/00A61Q19/00B01J2523/27B01J2523/31C07B41/02C07B63/00C07C2521/04C11D3/48
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Quick Facts
Patent No.
US 10,995,048
App. No.
16/682,059
Granted
May 4, 2021
Kind
B2
Abstract

A process is incorporated herein for the synthesis of bio-1,2-alkanediols, comprising: providing a bio-alkene having a carbon chain of about 5 to about 20 carbon atoms and a bio-1-alkene regioselectivity of at least about 80%, at least about 92% and/or at least about 95%; and converting the bio-alkene to a bio-1,2-alkanediol having a carbon chain length of about 5 to about 20 carbon atoms. Methods for treating catalysts which may be incorporated in the process for the synthesis of bio-1,2-alkanediols are also included herein. Such bio-1,2-alkanediols are used in compositions and products alone as antimicrobial materials, or with existing bio-compounds and/or antimicrobials, preservatives, alternative preservation systems and/or hurdle technology components. The bio-1,2-alkanediols incorporate a natural and bio-based pathway for antimicrobial effects in various compositions such as cosmetic, pharmaceutical, industrial and household products.

Claims (29)

1. A method for making a bio-alkene, comprising:

dehydrating a bio-1-alcohol by heating the bio-1-alcohol in a reactor with a catalyst, wherein the resulting bio-alkene has a carbon chain of about 5 to about 20 carbon atoms and a bio-1-alkene regioselectivity of at least about 80%.

2. The method of claim 1 , wherein the bio-alkene has a carbon chain of about 6 to about 14 carbon atoms.

3. The method according to claim 2 , wherein the bio-alkene has a carbon chain length of about 6 to about 10 carbon atoms.

4. The method according to claim 3 , wherein the bio-alkene has a carbon chain length of about 6 to about 8 carbon atoms.

5. The method according to claim 1 , wherein the bio-alkene is bio-octene.

6. The method according to claim 1 , wherein the reactor is a fixed bed reactor.

7. The method according to claim 6 , wherein the fixed bed reactor is a fluidized bed reactor.

8. The method according to claim 1 , wherein the catalyst is selected from ZnAl 2 O 4 and a -alumina catalyst.

9. The method according to claim 1 , wherein the bio-alkene has a bio-1-alkene regioselectivity of about 92% to about 99%.

10. The method according to claim 9 , wherein the bio-alkene has a bio-1-alkene regioselectivity of about 95% to about 99%.

11. The method according to claim 1 , wherein the catalyst is a γ-alumina catalyst is treated with a base to form a modified γ-alumina catalyst.

12. The method according to claim 11 , wherein the base comprises a Group I or a Group II metal.

13. The method according to claim 11 , wherein the γ-alumina catalyst is treated with a calcium promoter to provide a modified γ-alumina catalyst.

14. The method according to claim 13 , wherein the modified γ-alumina catalyst is calcined to provide a calcined γ-alumina catalyst.

15. The method according to claim 13 , wherein the calcium promoter is used in an amount of about 0.01 weight percent to about 4 weight percent based on the weight of CaO determined after calcination.

16. The method according to claim 15 , wherein the calcium promoter is used in an amount of about 1 weight percent to about 2 weight percent based on the weight of CaO determined after calcination.

17. The method according to claim 14 , wherein a temperature during calcination is about 400° C. to about 500° C.

18. The method according to claim 17 , wherein the temperature during calcination is about 420° C. to about 480° C.

19. The method according to claim 18 , wherein the temperature during calcination is about 440° C. to about 460° C.

20. The method according to claim 14 , wherein calcination is carried out in an oven.

21. The method according to claim 14 , wherein the calcination is carried out in an atmosphere of air or inert gas.

22. The method according to claim 1 , wherein the method comprises a distillation step to refine the bio-alkene.

23. The method according to claim 1 , wherein the bio-alkene results from a process wherein the bio-1-alcohol in water is dehydrated by heating the bio-1-alcohol with a catalyst under a purge gas.

24. The method according to claim 1 , wherein the bio-alkene is further reacted to form a bio-based compound different from the bio-alkene or a bio-based polymer.

25. The method according to claim 24 , wherein the bio-alkene is further reacted by a free radical or a catalytic polymerization process to form a bio-based polymer.

26. A bio-alkene made by the method of claim 1 .

27. The bio-alkene according to claim 26 , wherein the bio-alkene is selected from straight or branched chain bio-alkenes.

28. The bio-alkene according to claim 26 , wherein the resulting bio-1-alkene is selected from bio-1-pentene, bio-1-iso-pentene, bio-1-hexene, bio-1-heptene, bio-1-octene, bio-1-nonene, bio-1-decene, and bio-1-dodecene.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 2, 2020
From: BURGO, ROCCO V; WRIGHT, MICHAEL E; MOSSER, GARY B; FEVOLA, MICHAEL J
To: INOLEX INVESTMENT CORPORATION
Reel/Frame 051981/0661 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 5, 2019
From: BURGO, ROCCO V.; WRIGHT, MICHAEL E.; MOSSER, GARY B.; FEVOLA, MICHAEL J.
To: INOLEX INVESTMENT CORPORATION
Reel/Frame 051194/0088 →
Continuity (3)
Continuation 16262902 · Jan 30, 2019
Provisional Application 62623985 · Jan 30, 2018
Related Publication 20200189995A1 · Jun 18, 2020