Lignin depolymerisation and doxygenation process for obtaining aromatic compounds and their catalytic reaction composition

Patent metadata

Field	Value
Publication number	US-11180628-B2
Application number	US-201715843422-A
Country	US
Kind code	B2
Filing date	Dec 15, 2017
Priority date	Dec 15, 2016
Publication date	Nov 23, 2021
Grant date	Nov 23, 2021

Abstract

The present invention is related to a catalytic process, which includes catalytic compositions for depolymerisation and deoxygenation of lignin contained in the biomass for obtaining aromatic hydrocarbons. The catalytic composition consists of at least one non-noble element from group VIIIB of the periodic table supported on a mesoporous matrix composed of an inorganic oxide, which can be alumina surface-modified with a second inorganic oxide with the object of inhibiting the interaction between the active component and the support. The process of lignin depolymerisation consists of dissolving lignin in a mixture of protic liquids, reacting it|a reaction system by batch or in continuous flow at inert and/or reducing atmosphere, at a temperature of between 60 to 320° C. and a pressure of from 5 to 90 kg/cm 2 . When the reaction is developed into a batch system, oxygenated aromatic hydrocarbons are mainly produced, both by thermal as well as catalytic depolymerisation, whereas in a continuous flow reaction system, deoxygenated aromatic hydrocarbons are produced.

First claim

The invention claimed is:

1. A process of lignin depolymerisation and deoxygenation for obtaining aromatic compounds, the process comprising:
dissolving a lignin in a protic liquid, creating a dissolved protic lignin mixture that includes at least partially depolymerized lignin soluble in the protic liquid;
reacting the dissolved protic lignin mixture in a continuous flow reaction system at either an inert or reducing atmosphere, to form a dissolved lignin protic product, by passing a continuous flow of the dissolved protic lignin mixture mixed with at least one of an inert gas and a reducing gas through a fixed bed tubular reactor packed with a catalytic composition at a determined spatial time liquid hourly space velocity, pressure and temperature, the catalytic composition comprising a non-noble element of Group VIIIB of the periodic table, the non-noble element supported in a support material, the support material comprising a material selected from a group consisting of alumina, silica or a combination thereof; and
passing the dissolved lignin protic product through a cationic exchange resin followed by an anionic exchange resin in order to eliminate impurities, the impurities including a group of inorganic cations including Na, K and La and a group of ions including SO 4 and Cl;
wherein the determined reaction temperature is between 40° C. to 320° C., inclusive, the determined operation pressure is from 5 kg/cm 2 to 100 kg/cm 2 , inclusive; and
wherein reacting the dissolved protic lignin mixture in the continuous flow system produces a plurality of deoxygenated aromatic hydrocarbons by thermal and catalytic depolymerisation and deoxygenation.

2. The process according to claim 1 , wherein reacting the dissolved protic lignin mixture in the continuous flow system produces a plurality of deoxygenated aromatic hydrocarbons by thermal and catalytic depolymerization and deoxygenation.

3. The process according to claim 1 , wherein the dissolving a lignin comprises dissolving the lignin in a mixture of protic solvents placed in a container, creating a dissolved protic lignin mixture, and sealing the container; and wherein the reacting the dissolved protic lignin mixture comprises heating the dissolved protic lignin mixture at the determined reaction temperature, stirring the dissolved protic lignin mixture, and applying pressure with one of either an inert gas or hydrogen pressure to the reaction to maintain a set of determined reaction conditions for a determined reaction time.

4. The process according to claim 3 , wherein the applying pressure comprises adding an inert gas selected from the group consisting of helium, argon, and nitrogen, to reach the determined operation pressure.

5. The process according to claim 1 , wherein the determined operation pressure is between 5 kg/cm 2 and 50 kg/cm 2 , inclusive.

6. The process according to claim 1 , wherein the lignin is selected from a group containing sodium lignosulfonate, lignin Kraft, organosolv lignin, lignin obtained from lignocellulosic residues after the enzymatic hydrolysis of cellulose, lignin obtained directly from lignocellulosic residues, and black liqueur.

7. The process according to claim 1 , wherein the dissolved protic lignin mixture comprises a ratio of lignin to protic solvent of between 1 g/L to 100 g/L.

8. The process according to claim 1 , wherein the reaction system is packed with an inert material selected from a group consisting of quartz, alpha alumina and silicon carbide.

9. The process according to claim 1 , wherein the reaction is carried out at a reducing atmosphere with one of hydrogen or a mixture of hydrogen with inert gas.

10. The process according to claim 1 , wherein the reaction is carried out at an inert atmosphere, and wherein said determined operation pressure is between 5 kg/cm 2 to 50 kg/cm 2 , inclusive.

11. The process according to claim 1 , wherein the reaction is carried out at a hydrogen reducing atmosphere, and wherein the determined operation pressure is between 5 kg/cm 2 to 50 kg/cm 2 , inclusive.

12. The process according to claim 1 , wherein the reaction is thermally developed, further producing a plurality of oxygenated aromatic hydrocarbons.

13. The process according to claim 1 , wherein the process of lignin depolymerisation and deoxygenation further produces a plurality of oxygenated aromatic compounds in the presence of the catalytic composition.

14. A process of lignin depolymerisation and deoxygenation for obtaining aromatic compounds, the process comprising:
dissolving a lignin in a protic liquid, creating a dissolved protic lignin mixture that includes at least partially depolymerized lignin soluble in the protic liquid;
reacting the dissolved protic lignin mixture in a continuous flow reaction system at either an inert or reducing atmosphere, by passing it through a fixed bed reactor packed with a catalytic composition comprising a non-noble element of Group VIIIB of the periodic table, the non-noble element supported in a support material, the support material comprising a material selected from a group consisting of alumina, silica or a combination thereof;
wherein the reaction is carried out at a determined reaction temperature of between 40° C. to 320° C., inclusive, and a determined operation pressure of from 5 kg/cm 2 to 100 kg/cm 2 , inclusive, and the fixed bed tubular reactor is further packed with at least one inert material selected from the group consisting of quartz, alpha alumina and silicon carbide;
wherein reacting the dissolved protic lignin mixture in the continuous flow system produces a plurality of deoxygenated aromatic hydrocarbons by thermal and catalytic depolymerisation and deoxygenation.

15. The process according to claim 14 , wherein reacting the dissolved protic lignin mixture in the continuous flow system produces a plurality of deoxygenated aromatic hydrocarbons by thermal and catalytic depolymerization and deoxygenation.

16. The process according to claim 14 , wherein the dissolving a lignin comprises dissolving the lignin in a mixture of protic solvents placed in a container, creating a dissolved protic lignin mixture, and sealing the container; and wherein the reacting the dissolved protic lignin mixture comprises heating the dissolved protic lignin mixture at the determined reaction temperature, stirring the dissolved protic lignin mixture, and applying pressure with one of either an inert gas or hydrogen pressure to the reaction to maintain a set of determined reaction conditions for a determined reaction time.

17. The process according to claim 16 , wherein the applying pressure comprises adding an inert gas selected from the group consisting of helium, argon, and nitrogen, to reach the determined operation pressure.

18. The process according to claim 14 , wherein the determined operation pressure is between 5 kg/cm 2 and 50 kg/cm 2 , inclusive.

19. The process according to claim 14 , wherein the lignin is selected from a group containing sodium lignosulfonate, lignin Kraft, organosolv lignin, lignin obtained from lignocellulosic residues after the enzymatic hydrolysis of cellulose, lignin obtained directly from lignocellulosic residues, and black liqueur.

20. The process according to claim 14 , wherein the dissolved protic lignin mixture comprises a ratio of lignin to protic solvent of between 1 g/L to 100 g/L.

21. The process according to claim 14 , wherein the reaction is carried out at a reducing atmosphere with one of hydrogen or a mixture of hydro

Assignees

• Mexicano Inst Petrol

Inventors

• Toledo Antonio Jose Antonio
• Cortes Jacome Maria Antonia
• Mejia Centeno Isidro
• Garcia Martinez Jorge Alberto
• Escobar Aguilar Jose
• Lopez Salinas Esteban
• Mosqueira Mondragon Maria De Lourdes Araceli
• Perez Luna Miguel
• Angeles Chavez Carlos
• Sanchez Valente Jaime
• Guzman Castillo Maria De Lourdes Alejandra
• Medina Mendoza Ana Karina

Classifications

• B01J20/3204 Primary

  Inorganic carriers, supports or substrates · CPC title

• C07C41/00

  Preparation of ethers; Preparation of compounds having [IMAGE cpc-sch-C07C-0958.gif] groups,[IMAGE cpc-sch-C07C-0959.gif] groups or[IMAGE cpc-sch-C07C-0960.gif] groups · CPC title

• C07C45/59

  in five-membered rings (from ozonides C07C45/40) · CPC title

• C07C51/00

  Preparation of carboxylic acids or their salts, halides or anhydrides (of acids by hydrolysis of oils, fats or waxes C11C) · CPC title

• B01J29/0333

  Iron group metals or copper · CPC title