Catalytic method for the production of hydrocarbons and aromatic compounds from oxygenated compounds contained in aqueous mixtures

Patent metadata

Field	Value
Publication number	US-11839867-B2
Application number	US-201917058395-A
Country	US
Kind code	B2
Filing date	May 23, 2019
Priority date	May 25, 2018
Publication date	Dec 12, 2023
Grant date	Dec 12, 2023

Abstract

The present invention relates to a method for producing mixtures of hydrocarbons and aromatic compounds, for use as fuel components (preferably in the range C5-C16), by means of catalytic conversion of the oxygenated organic compounds contained in aqueous fractions derived from biomass treatments, wherein said method can comprise at least the following steps: (i) bringing the aqueous mixture containing the oxygenated organic compounds derived from biomass in contact with a catalyst comprising at least Sn and Nb, Sn and Ti, and combinations of Sn, Ti and Nb; (ii) reacting the mixture with the catalyst in a catalytic reactor at temperatures between 100 and 350° C. and under pressures from 1 to 80 bar in the absence of hydrogen; and (iii) recovering the products obtained by means of the liquid/liquid separation of the aqueous and organic phases.

First claim

The invention claimed is:

1. A method for producing mixtures of aliphatic hydrocarbons and aromatic compounds, the method comprising the following steps:
(a) bringing an aqueous mixture containing oxygenated organic compounds derived from primary treatments of biomass in contact with a catalyst, comprising at least one mixed metal oxide of Sn and Nb, Sn and Ti, and combinations of Sn, Ti and Nb, and which, in the calcined form thereof, is made up of at least 65% by weight of the rutile crystalline phase of SnO 2 ;
(b) reacting the mixture with the catalyst in a catalytic reactor at temperatures between 50° and 450° C. and under pressures from 1 to 120 bar in the absence of hydrogen; and
(c) recovering the products obtained in step (b) by means of a liquid/liquid separation of an aqueous and organic phases.

2. The method according to claim 1 , wherein the catalyst comprises the empirical formula:
Sn a Nb b Ti c M d O e

wherein:
M is a chemical element selected from the group consisting of transition metals, rare earth elements and lanthanides,
a is comprised between 0.05 and 10.0,
b and c are comprised between 0 and 10.0, wherein c+b is a value other than zero,
d is comprised between 0 and 4.0, and
e has a value which depends on the oxidation state of the elements Sn, Nb, Ti and the element M.

3. The method according to claim 2 , wherein d is zero and the catalyst comprises the empirical formula:
Sn a Nb b Ti c M d O e

wherein:
a is comprised between 0.05 and 10.0,
b and c are comprised between 0.05 and 10.0, and
e has a value which depends on the oxidation state of the elements Sn, Nb and Ti.

4. The method according to claim 2 , wherein c is zero and the catalyst comprises the empirical formula:
Sn a Nb b M d O e

wherein:
M is a chemical element selected from the group consisting of transition metals, rare earth elements and lanthanides,
a and b are comprised between 0.05 and 10,
d is comprised between 0 and 4.0, and
e has a value which depends on the oxidation state of the elements Sn, Nb and M.

5. The method according to claim 2 , wherein b is zero and the catalyst comprises the empirical formula:
Sn a Ti c M d O e

wherein:
M is a chemical element selected from the group consisting of transition metals, rare earth elements or lanthanides,
a and c are comprised between 0.05 and 10,
d is comprised between 0 and 4.0, and
e has a value which depends on the oxidation state of the elements Sn, Ti and M.

6. The method according to claim 1 , wherein the element M is a transition metal, lanthanide or rare earth element selected from the group consisting of V, Cr, Fe, Co, Ni, Cu, Zn, Mo, Ta, Ti, Re, La and combinations thereof.

7. The method according to claim 1 , wherein the oxygenated organic compounds have between 1 and 12 carbon atoms and between 1 and 9 oxygen atoms.

8. The method according to claim 1 , wherein a total concentration of the oxygenated organic compounds present in the aqueous mixture derived from the primary treatments of biomass is in a range between 0.5 and 99.5% by weight.

9. The method according to claim 8 , wherein a total concentration of the oxygenated organic compounds present in the aqueous mixture derived from the primary treatments of biomass is in a range between 1.0 and 70.0% by weight.

10. The method according to claim 1 , wherein the contact between the aqueous mixture and the catalyst is performed in a reactor selected from the group consisting of a batch reactor, a continuous stirred-tank reactor, a continuous fixed-bed reactor and a continuous fluidized-bed reactor.

11. The method according to claim 10 , wherein the reactor is a batch reactor and the reaction is carried out in the liquid phase.

12. The method according to claim 11 , wherein the process is carried out at a pressure between 1 to 80 bar.

13. The method according to claim 11 , wherein the process is performed at a temperature between 100° and 350° C.

14. The method according to claim 11 , wherein the contact between the aqueous mixture containing oxygenated organic compounds derived from the primary treatments of biomass and the catalyst is performed in a time ranging from 2 minutes to 200 hours.

15. The method according to claim 11 , wherein the weight ratio between the aqueous mixture containing the oxygenated organic compounds derived from the primary treatments of biomass and the catalyst is between 1 and 200.

16. The method according to claim 10 , wherein the reactor is a continuous fixed-bed reactor or a continuous fluidised-bed reactor, wherein the reaction temperature is comprised between 100° C. and 350° C.; the contact time is comprised between 0.001 and 200 s; and the working pressure is between 1 and 200 bar.

17. The method according to claim 1 , wherein the contact between the aqueous fraction containing oxygenated organic compounds and the catalyst is performed under an atmosphere made of nitrogen, argon, air, nitrogen-enriched air, argon-enriched air, or combinations thereof.

18. The method according to claim 17 , wherein the contact is performed in an atmosphere made of nitrogen.

Assignees

• Consejo Superior Investigacion
• Univ Valencia Politecnica
• Consejo Superior Investigacion

Inventors

• Domine Marcelo Eduardo
• Fernández-Arroyo Naranjo Alberto
• López Nieto José Manuel

Classifications

• B01J2235/15

  X-ray diffraction · CPC title

• B01J23/20 Primary

  Vanadium, niobium or tantalum · CPC title

• B01J8/001

  Controlling catalytic processes (B01J8/1809 takes precedence) · CPC title

• B01J8/02

  with stationary particles, e.g. in fixed beds · CPC title

• B01J8/24

  according to "fluidised-bed" technique (B01J8/20 takes precedence) · CPC title