US 12,221,405 B2
Pre-treatment of lignocellulosic feeds for the production of glycols
Jean Paul Andre Marie Joseph Ghislain Lange, Amsterdam (NL); Pieter Huizenga, Amsterdam (NL); Evert Van Der Heide, Amsterdam (NL); and Thimo Daniel Jozef Te Molder, Enschede (NL)
Assigned to SHELL USA, INC., Houston, TX (US)
Appl. No. 17/638,316
Filed by SHELL OIL COMPANY, Houston, TX (US)
PCT Filed Sep. 25, 2020, PCT No. PCT/EP2020/077013
§ 371(c)(1), (2) Date Feb. 25, 2022,
PCT Pub. No. WO2021/058808, PCT Pub. Date Apr. 1, 2021.
Claims priority of application No. 19199650 (EP), filed on Sep. 25, 2019.
Prior Publication US 2022/0298089 A1, Sep. 22, 2022
This patent is subject to a terminal disclaimer.
Int. Cl. C07C 29/60 (2006.01)
CPC C07C 29/60 (2013.01) 12 Claims
OG exemplary drawing
 
1. A process for the preparation of glycols from a lignocellulosic solid biomass comprising cellulose, hemicellulose and lignin in a reactor system, said process comprising:
a) contacting the lignocellulosic solid biomass with an organic solvent comprising a low boiling point alcohol, and a pre-treatment acid, at a temperature ranging from about 80 to about 220° C. and a pressure ranging from 1 to 50 bar (absolute) for a time ranging from about 5 minutes to about 2 hours to obtain a first mixture;
b) separating the first mixture obtained in step (a) into a pre-treated solid residue comprising cellulose and hemicellulose and a liquid stream comprising dissolved lignin;
c) subjecting the pre-treated solid residue to a hydrogenolysis reaction and generating a glycols stream, a lights stream and a heavies stream;
d) recycling at least a part of the lights stream to step (a), wherein the lights stream comprises a first portion of the organic solvent;
e) separating the liquid stream from step b) to produce a second portion of the organic solvent and a lignin stream; and
f) recycling at least a part of the second portion of the organic solvent to step (a),
wherein the first mixture has less than about 30 wt % water,
wherein the pre-treatment acid comprises at least one selected from the group consisting of: formic acid, acetic acid, propionic acid, butyric acid, glycolic acid, lactic acid, and combinations thereof which is/are at least partially generated in-situ in step (a); and
wherein the pre-treatment acid or a component of the pre-treatment acid is recycled to step (a).