Methods and systems for processing cellulosic biomass

Patent metadata

Field	Value
Publication number	US-9790432-B2
Application number	US-201514868435-A
Country	US
Kind code	B2
Filing date	Sep 29, 2015
Priority date	Oct 1, 2014
Publication date	Oct 17, 2017
Grant date	Oct 17, 2017

Abstract

Digestion of cellulosic biomass solids may be complicated by release of lignin therefrom. Methods and systems for processing a reaction product containing lignin-derived products, such as phenolics, can comprise hydrotreating the reaction product to convert the lignin-derived products to desired higher molecular weight compounds. The methods and systems can further include separating the higher molecular weight compounds from unconverted products, such as unconverted phenolics, and recycling the unconverted phenolics for use as at least a portion of the digestion solvent and for further conversion to desired higher molecular weight compounds with additional hydrotreatment. The methods and systems can further include a further hydrotreatment step configured for additional lignin conversion and/or a further hydrotreatment step configured for generating hydrogen.

First claim

The invention claimed is:

1. A method comprising:
providing a reactor in a first reaction zone with a first reaction content comprising cellulosic biomass solids, molecular hydrogen, a hydrogen-activating catalyst, and a digestion solvent;
heating the first reaction content in the reactor in the first reaction zone to form a first reaction product comprising phenolics and an alcoholic component;
providing a first reactor in a second reaction zone with a second reaction content comprising the first reaction product, molecular hydrogen, and a hydrogen-activating catalyst;
heating the second reaction content in the first reactor in the second reaction zone to form a second reaction product;
providing a second reactor in the second reaction zone with a third reaction content comprising the second reaction product, molecular hydrogen, and a hydrogen-activating catalyst;
heating the third reaction content in the second reactor in the second reaction zone to form a third reaction product comprising hydrocarbons converted from phenolics and unconverted phenolics;
separating an unconverted phenolics fraction from the third reaction product;
providing a first portion of the unconverted phenolics fraction to the reactor in the first reaction zone; and
providing a second portion of the unconverted phenolics fraction to at least one of the first reactor and the second reactor in the second reaction zone.

2. The method of claim 1 , wherein at least one of the second and third reaction contents has a concentration of phenolics of 50% or less by weight based on the total weight of the respective reaction content.

3. The method of claim 1 , wherein the second reaction content has a water concentration of at least 10% by weight based on the total weight of the second reaction content.

4. The method of claim 1 , wherein the unconverted phenolics fraction comprises greater than 50% of the amount of phenolics in the third reaction product from which the unconverted phenolics fraction is separated.

5. The method of claim 1 , wherein at least one of the first and second reactors in the second reaction zone has a pressure of less than 200 bar.

6. The method of claim 1 , wherein the alcoholic component comprises triols and glycol and wherein at least a portion of triols and glycol in the alcoholic component is converted to monohydric alcohols.

7. The method of claim 1 , wherein the first reaction content is heated to a temperature in a range of about 190 to 260 degrees C.

8. The method of claim 1 , wherein the second and third reaction contents are heated to a temperature in a range of about 210 to 300 degrees C.

9. The method of claim 1 , wherein the reactor in the first reaction zone has a total pressure of at least 30 bar.

10. The method of claim 1 , wherein the first and second reactors in the second reaction zone each has a total pressure of at least 30 bar.

11. The method of claim 1 , wherein at least one of the first and second reactors in the second reaction zone has a total pressure that is lower than a total pressure of the reactor in the first reaction zone.

12. The method of claim 1 , wherein the first reactor in the second reaction zone comprises an ebulatting bed reactor and the second reactor in the second reaction zone comprises a fixed bed reactor or a trickle bed reactor.

13. The method of claim 1 , wherein the hydrocarbons converted from phenolics comprise at least one of an alkane, an alkene, a cycloalkane, a cycloalkene, an alkyl derivative or substituent of the cycloalkane, and an alkenealkyl derivative or substituent of the cycloalkene.

14. The method of claim 1 , wherein the catalyst in at least one of the first and second reactors in the second reaction content comprises fluidly mobile catalyst particulates.

15. The method of claim 1 , wherein at least one of the first reaction zone and the second reaction zone comprises a slurry reactor.

16. The method of claim 1 , further comprising
increasing the catalytic activity in at least one of the first and second reactors in the second reaction zone to increase hydrogen generation.

Assignees

• Shell Oil Co

Inventors

• Powell Joseph Broun
• Chheda Juben Nemchand
• Joffrion Lamar Lane
• Anderson Philip Walter

Classifications

• C08H8/00

  Macromolecular compounds derived from lignocellulosic materials {(pretreatment thereof B27N)} · CPC title

• C10G3/42

  Catalytic treatment · CPC title

• C10G1/065 Primary

  in the presence of a solvent · CPC title

• C10G3/56

  suspended in the oil, e.g. slurries, ebullated beds · CPC title

• C10G2300/802

  Diluents · CPC title