IP Library Granted Patent US 9,382,489
Granted Patent B2
US 9,382,489 · App. 14/153,927 · Granted Jul 5, 2016

Renewable heating fuel oil

Inventors: Maria Magdalena Ramirez-Corredores (Houston, TX); Vicente Sanchez (Houston, TX); Changan Zhang (Houston, TX)
Assignee: Inaeris Technologies, LLC
C10L1/02C10G1/02C10G3/44C10G3/49C10G2300/1011C10G2400/06C10G2400/08C10L2290/02Y02P30/20
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Quick Facts
Patent No.
US 9,382,489
App. No.
14/153,927
Granted
Jul 5, 2016
Kind
B2
Abstract

More stable and valuable bio-oil produced from biomasses are provided. More specifically, more stable and valuable bio-oil useful as heating oil, alone or in combination with an oxygenated acyclic component, is provided. Particularly, various embodiments of the present invention provide for a bio-oil having sufficient heating value and stability to be useful as heating oil, alone or in combination with an oxygenated acyclic component, without the need to hydrotreat the bio-oil or use a similar deoxygenating process.

Claims (29)

1. A renewable heating fuel oil composition comprising:

a) a first component comprising a bio-oil derived from the thermochemical conversion of biomass, wherein the bio-oil comprises: i) an oxygenated component having an oxygen content of at least about 5 wt %, and ii) a non-oxygenated component having an aromatic content of at least about 25 wt %;

b) a second component comprising an oxygenated acyclic component comprising open chain molecules having 12 or more carbon atoms per molecule; and

wherein the renewable heating fuel oil composition has a heating value of at least about 14,000 Btu/lb.

2. The renewable heating fuel oil composition of claim 1 wherein the oxygen content of the oxygenated component of the bio-oil is from about 10 to about 30 wt %.

3. The renewable heating fuel oil composition of claim 1 wherein the oxygen content of the renewable heating fuel oil composition is from about 5 to about 30 wt %.

4. The renewable heating fuel oil composition of claim 1 wherein the aromatic content of the non-oxygenated component of the bio-oil is from about 30 to about 70 wt %.

5. The renewable heating fuel oil composition of claim 1 wherein the oxygenated component is present in the bio-oil in the range of from about 10 to about 90 wt %.

6. The renewable heating fuel oil composition of claim 1 wherein the non-oxygenated component is present in the bio-oil in the range of from about 20 to about 60 wt %.

7. The renewable heating fuel oil composition of claim 1 wherein the non-oxygenated aromatic content of the renewable heating fuel oil composition is from about 3 to about 60 wt %.

8. The renewable heating fuel oil composition of claim 1 wherein the non-oxygenated aromatic content of the renewable heating fuel oil composition is from about 25 to about 60 wt %.

9. The renewable heating fuel oil composition of claim 1 wherein the first component is present in the renewable heating fuel oil composition in the range of from about 50 to about 99 wt %; and wherein the second component is present in the renewable heating fuel oil composition in the range of from about 0.5 to about 50 wt %.

10. The renewable heating fuel oil composition of claim 1 wherein the bio-oil is present in the renewable heating fuel oil composition in the range of from about 60 to about 95 wt %; and wherein the oxygenated acyclic component is present in the renewable heating fuel oil composition in the range of from about 5 to about 40 wt %.

11. The renewable heating fuel oil composition of claim 1 wherein the second component is selected from the group consisting of: a fatty acid methyl ester (FAME), biodiesel, biomass-derived diesel, an at least partially upgraded bio-oil derived from the at least partial deoxygenation of a portion of the bio-oil, and combinations thereof.

12. The renewable heating fuel oil composition of claim 11 wherein the at least partially upgraded bio-oil comprises less than about 20 wt % oxygen.

13. The renewable heating fuel oil composition of claim 1 wherein the second component has a heating value of at least about 14,000 Btu/lb.

14. The renewable heating fuel oil composition of claim 1 wherein the open chain molecules having 12 or more carbon atoms per molecule are present in the second component in an amount of from about 70 to about 99 wt %.

15. The renewable heating fuel oil composition of claim 1 wherein the open chain molecules having 12 or more carbon atoms per molecule are present in the renewable heating fuel oil composition in an amount of from about 3 to about 50 wt %.

16. The renewable heating fuel oil composition of claim 1 wherein the renewable heating fuel oil composition is used as a fuel for a furnace, boiler, combustor, thermal oxidizer, turbine, or stove.

17. The renewable heating fuel oil composition of claim 1 wherein the thermochemical conversion of the biomass to produce the bio-oil does not include an oxygen-removing hydrotreatment step.

18. The renewable heating fuel oil composition of claim 1 having a stability parameter of less than about 15 cp/h.

19. The renewable heating fuel oil composition of claim 18 having a stability parameter of less than about 10 cp/h.

20. The renewable heating fuel oil composition of claim 1 having a heating value of at least about 15,000 Btu/lb.

21. The renewable heating fuel oil composition of claim 1 having a heating value of at least about 16,000 Btu/lb.

22. The renewable heating fuel oil composition of claim 1 wherein at least about 50 wt % of the renewable heating fuel oil composition has a boiling point from about 180° C. to about 380° C.

23. The renewable heating fuel oil composition of claim 1 wherein at least about 60 wt % of the renewable heating fuel oil composition has a boiling point from about 180° C. to about 380° C.

24. The renewable heating fuel oil composition of claim 1 wherein the bio-oil is produced by a process comprising:

a) converting at least a portion of the biomass in an oxygen-poor environment in the presence of a catalyst material at a temperature in the range of from about 200° C. to about 1000° C. to produce a reaction product stream containing the bio-oil; and

b) separating the bio-oil from the reaction product stream; wherein steps a) and b) do not include an oxygen-removing hydrotreatment step.

Assignments (5)
CHANGE OF NAME Recorded Aug 18, 2020
From: INAERIS TECHNOLOGIES, LLC
To: MARD, INC.
Reel/Frame 054213/0032 →
CHANGE OF NAME Recorded Apr 7, 2016
From: KIOR, LLC
To: INAERIS TECHNOLOGIES, LLC
Reel/Frame 038380/0344 →
NUNC PRO TUNC ASSIGNMENT Recorded Sep 29, 2015
From: KIOR, INC.
To: KIOR, LLC
Reel/Frame 036717/0262 →
SECURITY INTEREST Recorded Jul 22, 2014
From: KIOR, INC.
To: KFT TRUST, VINOD KHOSLA, TRUSTEE, AS FIRST LIEN AGENT
Reel/Frame 033390/0423 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 24, 2014
From: RAMIREZ-CORREDORES, MARIA MAGDALENA; SANCHEZ, VICENTE; ZHANG, CHANGAN
To: KIOR, INC.
Reel/Frame 032510/0983 →
Continuity (5)
Continuation In Part 13025483 · Feb 11, 2011
Continuation In Part 13964873 · Aug 12, 2013
Continuation In Part 13533432 · Jun 26, 2012
Continuation 12915872 · Oct 29, 2010
Related Publication 20140123545A1 · May 8, 2014